WO2013031675A1 - Membrane électrolyte polymère, ensemble électrode à membrane qui utilise cette dernière et pile à combustible à polymère solide - Google Patents

Membrane électrolyte polymère, ensemble électrode à membrane qui utilise cette dernière et pile à combustible à polymère solide Download PDF

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WO2013031675A1
WO2013031675A1 PCT/JP2012/071408 JP2012071408W WO2013031675A1 WO 2013031675 A1 WO2013031675 A1 WO 2013031675A1 JP 2012071408 W JP2012071408 W JP 2012071408W WO 2013031675 A1 WO2013031675 A1 WO 2013031675A1
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group
ionic group
electrolyte membrane
segment
polymer electrolyte
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PCT/JP2012/071408
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Japanese (ja)
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浩明 梅田
大輔 出原
絵美 天野
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東レ株式会社
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Priority to JP2012539113A priority Critical patent/JP5338990B2/ja
Priority to CA2847107A priority patent/CA2847107C/fr
Priority to CN201280041595.4A priority patent/CN103782434B/zh
Priority to EP12826803.4A priority patent/EP2752928B1/fr
Priority to US14/240,754 priority patent/US20140322628A1/en
Priority to KR1020147005472A priority patent/KR101409059B1/ko
Publication of WO2013031675A1 publication Critical patent/WO2013031675A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/38—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols
    • C08G65/40—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols from phenols (I) and other compounds (II), e.g. OH-Ar-OH + X-Ar-X, where X is halogen atom, i.e. leaving group
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018—Polymeric electrolyte materials
    • H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018—Polymeric electrolyte materials
    • H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
    • H01M8/1023—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having only carbon, e.g. polyarylenes, polystyrenes or polybutadiene-styrenes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/38—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols
    • C08G65/40—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols from phenols (I) and other compounds (II), e.g. OH-Ar-OH + X-Ar-X, where X is halogen atom, i.e. leaving group
    • C08G65/4012—Other compound (II) containing a ketone group, e.g. X-Ar-C(=O)-Ar-X for polyetherketones
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/48—Polymers modified by chemical after-treatment
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/20—Manufacture of shaped structures of ion-exchange resins
    • C08J5/22—Films, membranes or diaphragms
    • C08J5/2206—Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
    • C08J5/2218—Synthetic macromolecular compounds
    • C08J5/2256—Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions other than those involving carbon-to-carbon bonds, e.g. obtained by polycondensation
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
    • H01B1/06—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances
    • H01B1/12—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances organic substances
    • H01B1/122—Ionic conductors
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2650/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G2650/28—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type
    • C08G2650/38—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type containing oxygen in addition to the ether group
    • C08G2650/40—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type containing oxygen in addition to the ether group containing ketone groups, e.g. polyarylethylketones, PEEK or PEK
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/38—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols
    • C08G65/40—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols from phenols (I) and other compounds (II), e.g. OH-Ar-OH + X-Ar-X, where X is halogen atom, i.e. leaving group
    • C08G65/4012—Other compound (II) containing a ketone group, e.g. X-Ar-C(=O)-Ar-X for polyetherketones
    • C08G65/4043—(I) or (II) containing oxygen other than as phenol or carbonyl group
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2371/00—Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
    • C08J2371/08—Polyethers derived from hydroxy compounds or from their metallic derivatives
    • C08J2371/10—Polyethers derived from hydroxy compounds or from their metallic derivatives from phenols
    • C08J2371/12—Polyphenylene oxides
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M2008/1095—Fuel cells with polymeric electrolytes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells

Definitions

  • the present invention provides a polymer electrolyte having excellent proton conductivity even under low humidification conditions and low temperature conditions, and excellent practicality capable of achieving excellent mechanical strength, fuel cutoff and long-term durability.
  • the present invention relates to a membrane, a membrane electrode assembly using the membrane, and a polymer electrolyte fuel cell.
  • a fuel cell is a kind of power generation device that extracts electric energy by electrochemically oxidizing a fuel such as hydrogen or methanol, and has recently attracted attention as a clean energy supply source.
  • the polymer electrolyte fuel cell has a standard operating temperature as low as around 100 ° C. and a high energy density, so that it is a relatively small-scale distributed power generation facility, a mobile power generator such as an automobile or a ship.
  • a mobile power generator such as an automobile or a ship.
  • secondary batteries such as nickel metal hydride batteries and lithium ion batteries.
  • an anode electrode and a cathode electrode in which a reaction responsible for power generation occurs, and a polymer electrolyte membrane serving as a proton conductor between the anode and the cathode are sometimes referred to as a membrane electrode assembly (hereinafter, abbreviated as MEA).
  • MEA membrane electrode assembly
  • a cell in which this MEA is sandwiched between separators is configured as a unit.
  • the polymer electrolyte membrane is mainly composed of a polymer electrolyte material.
  • the polymer electrolyte material is also used as a binder for the electrode catalyst layer.
  • the polymer electrolyte membrane As a required characteristic of the polymer electrolyte membrane, firstly, high proton conductivity is mentioned. In addition, since the polymer electrolyte membrane also functions as a barrier that prevents direct reaction between fuel and oxygen, low permeability of the fuel is required. Other necessary characteristics include chemical stability to withstand a strong oxidizing atmosphere during fuel cell operation, mechanical strength that can withstand repeated thinning and swelling and drying, and physical durability.
  • Nafion registered trademark
  • DuPont which is a perfluorosulfonic acid polymer
  • Nafion registered trademark
  • the fuel crossover fuel permeation amount
  • problems such as loss of mechanical strength and physical durability of the membrane due to swelling and drying, problems of low softening point and inability to use at high temperatures, problems of disposal treatment after use and difficulty in recycling materials are pointed out. It has been.
  • Patent Documents 1 to 3 disclose a block copolymer having a segment not containing a sulfonic acid group and a segment containing a sulfonic acid group, the phase separation structure of which is a series of polymers exhibiting a lamellar or co-continuous structure. Proposed.
  • Patent Documents 4 and 5 describe block copolymers in which the segment is composed of a tough aromatic polyetherketone (PEK) system.
  • PEK polyetherketone
  • Japanese Unexamined Patent Publication No. 2005-190830 Japanese Unexamined Patent Publication No. 2005-216525 Japanese Unexamined Patent Publication No. 2011-023308 Japanese Unexamined Patent Publication No. 2005-126684 International Publication No. 2008-018487 Pamphlet
  • Patent Documents 1 to 3 are effective in lamellar and co-continuous structures in terms of improving proton conductivity while maintaining an appropriate density of sulfonic acid groups. Since a high amorphous polymer is used for the basic skeleton, it is easily brittle and inferior in physical durability. In addition, hot water resistance and physical durability degradation due to the inclusion of many sulfonic acid groups with high water absorption were further cited as problems.
  • Patent Document 4 lists, as a preferred example, block copolymers in which the former segment is PEK and the latter segment is sulfonated polyetheretherketone.
  • the former segment is PEK
  • the latter segment is sulfonated polyetheretherketone.
  • the block copolymer was not examined in detail including the phase separation structure. .
  • the electron density between the ether group and the ether group is high and includes a highly reactive phenylene group or biphenylene group, and sulfonic acid is introduced into these activated groups, oxidation degradation and The chemical stability against desulfonation was insufficient.
  • Patent Document 5 an electrolyte membrane made of a block copolymer of aromatic PEK obtained by a production method through protection and deprotection of a ketone moiety, a high proton due to its crystallinity and phase separation structure. Confirmed conductivity. However, because the linker is not used, the polymerization temperature rises, and side reactions such as randomization by ether exchange and segment cleavage proceed partially, so that the phase separation structure exhibited by the electrolyte membrane may not be uniform. In addition, no co-continuous or lamellar-like structure was observed, and higher low-humidity proton conductivity could not be realized.
  • the polymer electrolyte membrane in the prior art is insufficient as a means for improving economy, workability, proton conductivity, mechanical strength, chemical stability, and physical durability, and is industrially useful. It could not be a polymer electrolyte membrane.
  • the present invention has excellent proton conductivity even under low humidification conditions and low temperature conditions, and is excellent in mechanical strength and fuel cutoff performance. Therefore, it is an object of the present invention to provide a polymer electrolyte membrane that can achieve high output, high energy density, and long-term durability, and a membrane electrode assembly and a polymer electrolyte fuel cell using the polymer electrolyte membrane.
  • the polymer electrolyte membrane of the first invention is a polymer electrolyte comprising a block copolymer containing one or more segments (A1) containing ionic groups and one or more segments (A2) containing no ionic groups.
  • the film has a co-continuous or lamellar-like phase separation structure, and the crystallization calorific value measured by differential scanning calorimetry is 0.1 J / g or more, or wide-angle X-ray diffraction The crystallinity measured by is characterized by being 0.5% or more.
  • the polymer electrolyte membrane of the second aspect of the present invention is a polymer electrolyte membrane comprising a block copolymer containing one or more segments (A1) containing ionic groups and one or more segments (A2) containing no ionic groups.
  • segment (A2) which forms a co-continuous or lamellar phase separation structure and does not contain an ionic group is composed of a repeating unit represented by the following general formula (Q1) To do.
  • Z 1 and Z 2 in the general formula (Q1) each represent a divalent organic group containing an aromatic ring, and each may represent two or more groups, but do not include an ionic group. Each independently represents a positive integer.
  • the membrane electrode assembly and the polymer electrolyte fuel cell of the present invention are characterized by comprising such a polymer electrolyte membrane.
  • the membrane electrode assembly using the polymer electrolyte membrane, and the polymer electrolyte fuel cell it has excellent proton conductivity even under low humidification conditions, and has mechanical strength and chemical stability.
  • the polymer electrolyte fuel cell can achieve high output and excellent physical durability.
  • (A)-(d) is explanatory drawing which shows typically the aspect of the phase-separation structure in a polymer electrolyte membrane, (a) is co-continuous, (b) is lamellar, (c) is a cylinder structure , (D) illustrates a sea-island structure.
  • the present invention has excellent proton conductivity even under the above-mentioned problems, that is, low humidification and low temperature conditions, and is excellent in mechanical strength and fuel shut-off property.
  • the proton conductivity of polymer electrolyte membranes is a phase-separated structure, that is, a segment containing an ionic group (A1) And highly dependent on the higher order structure and shape of the block copolymer having segment (A2) that does not contain ionic groups, as well as the stability of the higher order structure of the polymer in terms of mechanical strength, fuel barrier properties, and long-term durability. It has been found that it greatly depends on the property, that is, the packing property of the polymer, the crystallinity and the crystalline / amorphous state.
  • the polymer electrolyte membrane is composed of a block copolymer containing at least one segment (A1) containing an ionic group and at least one segment (A2) containing no ionic group.
  • the phase separation structure is formed, and the heat of crystallization measured by differential scanning calorimetry is 0.1 J / g or more, or the crystallinity measured by wide-angle X-ray diffraction is 0.1.
  • a polymer electrolyte membrane comprising a block copolymer containing at least one segment containing an ionic group (A1) and one segment containing no ionic group (A2).
  • segment (A2) that forms a co-continuous or lamellar phase separation structure and does not contain an ionic group is composed of a repeating unit represented by the following general formula (Q1) It is obtained by investigation to solve at once such problems in.
  • Z 1 and Z 2 in the general formula (Q1) each represent a divalent organic group containing an aromatic ring, and each may represent two or more groups, but do not include an ionic group. Each independently represents a positive integer.
  • the block copolymer represents a block copolymer composed of two or more types of segments, and the segment is a partial structure in the block copolymer, and one type of repeating unit. Or it consists of a combination of a plurality of types of repeating units and represents a molecular weight of 2000 or more.
  • the polymer electrolyte membrane of the present invention is composed of a block copolymer comprising a segment (A2) not containing an ionic group together with a segment (A1) containing an ionic group.
  • segment not containing a group means that the segment (A2) may contain a small amount of an ionic group as long as the effect of the present invention is not adversely affected.
  • does not contain an ionic group may be used in the same meaning.
  • the polymer electrolyte membrane of the present invention is characterized in that the phase separation structure is co-continuous or lamellar, but the phase separation structure is a polymer composed of two or more types of incompatible segments, for example, the ion It can be expressed in a polymer composed of a block copolymer having a segment (A1) containing a functional group and a segment (A2) not containing an ionic group, and its structural aspect is largely co-continuous (M1), lamellar (M2), cylinder (M3), and sea island (M4).
  • the light continuous phase is formed by one segment selected from the segment (A1) containing an ionic group and the segment (A2) containing no ionic group, and has a dark color.
  • the continuous or dispersed phase is formed by the other segment.
  • both the segment (A1) containing an ionic group and the segment (A2) containing no ionic group form a continuous phase.
  • phase separation structures are described in, for example, Annual Review of Physical Chemistry, 41, 1990, p.525.
  • excellent proton conductivity can be realized even under low humidification and low temperature conditions.
  • the structure is (M1), (M2) shown in FIG. 1, that is, a structure composed of co-continuous (M1) or lamellar (M2)
  • a continuous proton conducting channel is formed at the same time.
  • a polymer that has not only excellent proton conductivity, but also excellent fuel barrier properties, solvent resistance, mechanical strength, and physical durability compared to the crystallinity of the domain (A2) that does not contain an ionic group.
  • An electrolyte membrane may be feasible.
  • a co-continuous (M1) phase separation structure is particularly preferred.
  • a continuous proton conduction channel can be formed even in the case of the phase separation structure of (M3), (M4), that is, the cylinder structure (M3) and the sea-island structure (M3) shown in FIG.
  • the ratio of the segment (A1) containing an ionic group is relatively small compared to the segment (A2) containing no ionic group, or the segment (A2) containing no ionic group
  • the structure can be constructed when the ratio is relatively small with respect to the segment (A1) containing an ionic group, particularly for a diblock polymer in which two different segments are linked one by one. Has been. In the former case, the amount of ionic groups responsible for proton conduction is absolutely reduced.
  • the continuous proton conduction channel itself is not formed, so the proton conductivity is inferior. In the latter case, the proton conduction is excellent. However, since there are few crystalline nonionic domains, it is inferior in fuel-blocking property, solvent resistance, mechanical strength, and physical durability, and the effect of this invention is not fully acquired.
  • the domain means a lump formed by aggregating similar segments in one or a plurality of polymer chains.
  • having a co-continuous-like (M1) or lamellar-like (M2) phase separation structure is defined as having the structure when a desired image is observed by the following method.
  • a three-dimensional view of a digital slice cut out from three directions of length, width, and height is compared with a three-dimensional view obtained by TEM tomography observation.
  • the phase separation structure is in the case of continuous-like (M1) or lamellar-like (M2), the hydrophilic domain containing (A1) and the hydrophobic domain containing (A2) together form a continuous phase in all three views.
  • each of the continuous phases shows a complicated pattern
  • a pattern in which the layers are continuous is shown.
  • the continuous phase means a phase in which individual domains are connected without being isolated from each other macroscopically, but there may be a part that is not partially connected.
  • a polymer in order to clarify the aggregation state and contrast of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group, a polymer is added in a 2% by weight lead acetate aqueous solution.
  • the ionic group is ion-exchanged with lead, and then subjected to transmission electron microscope (TEM) and TEM tomography observation.
  • TEM transmission electron microscope
  • the polymer electrolyte membrane of the present invention needs to have crystallinity, crystallinity needs to be recognized by differential scanning calorimetry (DSC) or wide angle X-ray diffraction. That is, one embodiment of the polymer electrolyte membrane of the present invention is a polymer electrolyte membrane (hereinafter, referred to as embodiment A) having a crystallization calorific value measured by differential scanning calorimetry of not less than 0.1 J / g. .), And another embodiment is a polymer electrolyte membrane (hereinafter sometimes referred to as embodiment B) having a crystallinity of 0.5% or more as measured by wide-angle X-ray diffraction. In the present invention, both of the embodiments A and B are preferable embodiments, but the embodiment A is more preferable from the viewpoint of high toughness and durability.
  • “having crystallinity” means that the polymer can be crystallized when the temperature rises, has a crystallizable property, or has already been crystallized.
  • An amorphous polymer means a polymer that is not a crystalline polymer and that does not substantially proceed with crystallization. Therefore, even if it is a crystalline polymer, if the crystallization is not sufficiently advanced, the polymer may be in an amorphous state.
  • the aspect A of the polymer electrolyte membrane of the present invention requires that the crystallization heat amount ⁇ H per unit weight [g] of the dry polymer measured by differential scanning calorimetry (DSC) is 0.1 J / g or more. is there.
  • DSC differential scanning calorimetry
  • a temperature modulation DSC can be more preferably used in terms of measurement accuracy.
  • ⁇ H is more preferably 2 J / g or more from the viewpoint of mechanical strength, long-term durability, and fuel cutoff.
  • ⁇ H is more preferably 5 J / g or more, further preferably 10 J / g or more, and most preferably 15 J / g or more.
  • the upper limit of ⁇ H is not particularly limited, but 500 J / g or less is a realistic value.
  • the crystallization heat amount ⁇ H of the polymer electrolyte membrane of the present invention is:
  • the evaluation is based on the area of the crystallization peak measured when crystals are formed at the first temperature rise.
  • the crystallization heat amount ⁇ H needs to be 0.1 J / g or more.
  • thermogravimetric differential thermal simultaneous measurement TG-DTA
  • crystallize by raising the temperature to below the thermal decomposition temperature.
  • peaks If a crystallization peak is observed above the thermal decomposition temperature, the chemical structure of the polymer may have changed, and it cannot be determined that the polymer had crystallinity.
  • the polymer electrolyte membrane in which a crystallization peak is observed at the first temperature rise has crystallinity.
  • a polymer electrolyte membrane made of an amorphous polymer does not show a crystallization peak by differential scanning calorimetry.
  • embodiment A having an amorphous portion where crystallization proceeds with increasing temperature is a preferred example.
  • the presence of an amorphous part where crystals are generated and crystallized at a high temperature makes it not only excellent in proton conductivity and fuel barrier properties, but also extremely excellent in solvent resistance, mechanical strength and physical durability. There are cases where it is possible.
  • the presence / absence of crystallization peak and the crystallization calorimetry of the ionic group-containing block copolymer by temperature modulation DSC are carried out by the methods described in Examples.
  • the thermal decomposition temperature is preferably confirmed separately by TG-DTA measurement or the like.
  • the crystallization peak when the polymer is heated is observed in an irreversible process, and the temperature is observed above the glass transition temperature and below the melting temperature.
  • the amount of crystallization heat can be calculated from the area of the crystallization peak.
  • the crystallization temperature, the thermal decomposition temperature, and the melting temperature are close, and the high temperature side of the crystallization peak is
  • a value obtained by doubling the amount of heat from the low temperature side to the peak top is defined as the amount of crystallization heat.
  • the crystallinity measured by wide-angle X-ray diffraction needs to be 0.5% or more.
  • the degree of crystallinity of the polymer electrolyte membrane of the present invention can be evaluated by the crystallinity measured by wide-angle X-ray diffraction, and in particular, from the viewpoint of dimensional stability, mechanical strength, and long-term durability, The degree of conversion is more preferably 3% or more, and further preferably 5% or more.
  • the upper limit of the crystallinity is not particularly limited, but 50% or less is a realistic value.
  • the polymer is amorphous, structurally unstable and lacks dimensional stability. Or toughness may be insufficient and long-term durability may be insufficient.
  • the polymer is already crystallized with a polymer electrolyte membrane that is amorphous without having crystallinity.
  • a polymer electrolyte membrane that has already been crystallized becomes the embodiment B of the polymer electrolyte membrane of the present invention, and has a crystallinity of 0.5% or more by wide-angle X-ray diffraction.
  • a polymer electrolyte membrane made of an amorphous polymer has an unstable structure, so that sufficient dimensional stability, mechanical strength, physical durability, fuel barrier properties, and solvent resistance cannot be obtained. High energy capacity and long-term durability cannot be achieved when used in batteries.
  • an aromatic polyether polymer containing a ketone group that is, the following general formula (Q1) ), which does not contain an ionic group.
  • Z 1 and Z 2 in the general formula (Q1) each represent a divalent organic group containing an aromatic ring, and each may represent two or more groups, but do not include an ionic group. Each independently represents a positive integer.
  • the high planarity of the ketone group due to the sp2 carbon and the high polarizability of carbon-oxygen improve the packing property between the molecular chains, so that this skeleton can be incorporated into a segment of the block copolymer that does not contain an ionic group.
  • a polymer electrolyte membrane having sufficient dimensional stability, mechanical strength, physical durability, fuel barrier properties, and solvent resistance can be obtained.
  • Preferred organic groups as Z 1 and Z 2 in the general formula (Q1) include Z 1 as a phenylene group and Z 2 as the following general formulas (X-1), (X-2), (X-4) , (X-5) is more preferable. Moreover, although you may substitute by groups other than an ionic group, the direction where it is unsubstituted is more preferable at the point of crystallinity provision.
  • Z 1 and Z 2 are more preferably a phenylene group, and most preferably a p-phenylene group. (The groups represented by the general formulas (X-1), (X-2), (X-4), (X-5) may be optionally substituted with a group other than an ionic group).
  • the structural unit represented by the general formula (Q1) include structural units represented by the following general formulas (Q2) to (Q7), but are not limited thereto. It is possible to select appropriately in consideration of crystallinity and mechanical strength. Among these, from the viewpoint of crystallinity and production cost, the structural unit represented by the general formula (Q1) is more preferably the following general formulas (Q2), (Q3), (Q6), and (Q7). Formulas (Q2) and (Q7) are most preferable. (General formulas (Q2) to (Q7) are all represented in the para position, but may have other bonding positions such as ortho and meta positions as long as they have crystallinity. The para position is more preferable from the viewpoint of
  • the period length of the phase-separated structure comprising a block copolymer containing at least one segment (A1) containing an ionic group and one (A2) containing no ionic group according to the present invention is determined by a transmission electron microscope (TEM). )
  • the average value estimated from the autocorrelation function given by the image processing of the phase separation structure obtained by observation is preferably in the range of 2 to 200 nm, and has proton conductivity, mechanical strength, and physical durability. From the viewpoint, 5 nm or more is more preferable. Moreover, 100 nm or less is more preferable.
  • the period length is other than the above, that is, smaller than 2 nm, the phase separation structure becomes unclear and a good proton conduction channel may not be formed.
  • it is larger than 200 nm although a proton conduction channel is formed, it may be inferior in mechanical strength and physical durability due to swelling.
  • Observation of the phase separation structure of the polymer electrolyte membrane by a transmission electron microscope (TEM) and TEM tomography, image processing thereof, and calculation of the period length are performed by the method described in the examples.
  • TEM transmission electron microscope
  • the electrolyte material included in the polymer electrolyte membrane in which the phase separation structure is observed by TEM and TEM tomography of the present invention includes a segment (A1) containing an ionic group and a segment (A2) containing no ionic group, respectively.
  • a suitable example is a polymer mixture in which a polymer or oligomer containing an ionic group and / or a polymer or oligomer containing no ionic group is added to the block copolymer in addition to the block copolymer containing one or more. However, it is possible to use it without being limited to these.
  • the block copolymer further contains one or more linker sites that connect the segments (A1) and (A2).
  • the linker is a site connecting the segment (A1) containing an ionic group and the segment (A2) containing no ionic group, and contains a segment (A1) containing an ionic group. And a segment having a different chemical structure from the segment (A2) not containing an ionic group.
  • This linker enables the linkage between different segments while suppressing randomization, segment cleavage and side reactions due to the ether exchange reaction. Necessary for developing a phase separation structure. In the absence of a linker, segment cleavage such as randomization may occur, and the effects of the present invention may not be sufficiently obtained.
  • Two or more kinds of mutually incompatible segment chains that is, a hydrophilic segment containing an ionic group and a hydrophobic segment not containing an ionic group are linked by a linker site to form a polymer chain.
  • phase separation is performed into nano- or micro-domains composed of respective segment chains by short-range interaction resulting from repulsion between chemically different segment chains.
  • each domain is arranged with a specific order.
  • An object of the present invention is to obtain a polymer electrolyte membrane having excellent proton conductivity.
  • the polymer electrolyte membrane of the present invention can be obtained by appropriately selecting the chemical structure, segment chain length, molecular weight, ion exchange capacity, etc. of the block copolymer, thereby allowing processability, domain size, crystalline / amorphous, mechanical strength, Various characteristics such as fuel barrier properties, proton conductivity, and dimensional stability can be controlled.
  • the polymer electrolyte membrane of the present invention controls amorphous / crystallinity by introducing / deprotecting protecting groups, and imparts crystallinity to the ionic group-containing block copolymer used.
  • the high-order structure stability of the segment is enhanced by the pseudo-crosslinking effect, and it has excellent proton conductivity under low humidification conditions and low temperature conditions, yet has excellent dimensional stability, fuel cutoff, mechanical strength and physical properties. Durability was achieved.
  • the domain containing the segment (A1) containing an ionic group plays a role of increasing proton conductivity by forming a proton conduction channel
  • the domain containing the segment (A2) containing no ionic group is based on strong crystallinity.
  • the pseudo-crosslinking effect serves to enhance the performance of dimensional stability, fuel cutoff, mechanical strength and long-term durability. That is, according to the present invention, parts having different functions of ion conductivity and crystallinity are blocked and a phase separation structure is formed to separate the functions, thereby achieving both power generation performance and durability.
  • linker capable of suppressing randomization by ether exchange, segment cleavage and side reactions.
  • the ionic group-containing block copolymer used in the present invention is more preferably a hydrocarbon polymer from the viewpoint of crystallinity and mechanical strength.
  • the ionic group-containing hydrocarbon polymer referred to in the present invention means a polymer having an ionic group other than a perfluoro polymer.
  • the perfluoro polymer means a polymer in which most or all of the hydrogen of the alkyl group and / or alkylene group in the polymer is substituted with fluorine atoms.
  • a polymer in which 85% or more of hydrogen of an alkyl group and / or an alkylene group in a polymer is substituted with a fluorine atom is defined as a perfluoro polymer.
  • perfluoro polymers having an ionic group include Nafion (registered trademark) (manufactured by DuPont), Flemion (registered trademark) (manufactured by Asahi Glass Co., Ltd.), and Aciplex (registered trademark) (Asahi Kasei). (Commercially available).
  • the structure of the perfluoro polymer having these ionic groups can be represented by the following general formula (N1). [In Formula (N1), n1 and n2 each independently represents a natural number. k1 and k2 each independently represents an integer of 0 to 5. ]
  • perfluoro polymers having an ionic group form a clear phase structure in which the hydrophobic portion and the hydrophilic portion in the polymer form a water channel, so that a water channel called a cluster is formed in the polymer in a water-containing state. It is easy to move fuel such as methanol in the water channel, and reduction in fuel crossover cannot be expected. Also, because of the bulky side chain, crystallinity is not recognized, which is not preferable.
  • the ionic group-containing block copolymer used in the present invention is more preferably a polymer having an aromatic ring in the main chain among hydrocarbon polymers from the viewpoint of mechanical strength, physical durability and chemical stability. That is, it is a polymer having an aromatic ring in the main chain and having an ionic group.
  • the main chain structure is not particularly limited as long as it has an aromatic ring, but a main chain structure having sufficient mechanical strength and physical durability, for example, used as an engineering plastic is preferable.
  • Polysulfone, polyethersulfone, polyetherketone, etc., as used herein are generic terms for polymers having a sulfone bond, an ether bond, or a ketone bond in the molecular chain.
  • Polyetherketoneketone, polyetheretherketone, polyketone It includes ether ether ketone ketone, polyether ketone ether ketone ketone, polyether ketone sulfone, etc. and does not limit the specific polymer structure.
  • polysulfone, polyethersulfone, polyphenylene oxide, polyarylene ether-based polymer, polyphenylene sulfide, polyphenylene sulfide sulfone, polyarylene ketone, polyether ketone, polyarylene phosphine oxide, poly Polymers such as ether phosphine oxide are more preferred from the viewpoints of mechanical strength, physical durability, processability and hydrolysis resistance.
  • a polymer containing an aromatic group in the main chain having a repeating unit represented by the following general formula (T1) can be given.
  • Z 1 and Z 2 each represents an organic group containing an aromatic ring, and each may represent two or more groups. At least one of Z 1 and Z 2 is ionic.
  • Y 1 represents an electron-withdrawing group
  • Y 2 represents O or S.
  • a and b each independently represent 0 or a positive integer, provided that a and b are not 0 at the same time.
  • the polymers having the repeating units represented by the general formula (T1-1) to the general formula (T1-6) are resistant. It is more preferable in terms of hydrolyzability, mechanical strength, physical durability and production cost. Among them, from the viewpoint of mechanical strength, physical durability, and production cost, an aromatic polyether polymer in which Y 2 is O is more preferable, and the repeating unit represented by the general formula (T1-3) is most preferable. Most preferred are aromatic polyetherketone polymers in which Y 1 is a —CO— group, Y 2 is O, and a and b are independent positive integers.
  • Z 1 and Z 2 each represents an organic group containing an aromatic ring, and each may represent two or more groups. At least one of Z 1 and Z 2 is ionic.
  • a and b each independently represents 0 or a positive integer, provided that a and b are not simultaneously 0.
  • R p is an organic group.
  • Preferred organic groups as Z 1 and Z 2 are a phenylene group, a naphthylene group, and a biphenylenic group. These include those containing ionic groups. Moreover, although you may substitute by groups other than an ionic group, the direction where it is unsubstituted is more preferable at the point of crystallinity provision. Further, a phenylene group having a phenylene group and an ionic group is preferable, and a p-phenylene group having a p-phenylene group and an ionic group is most preferable.
  • Preferred examples of the organic group represented by R p in the general formula (T1-4) include a methyl group, an ethyl group, a propyl group, an isopropyl group, a cyclopentyl group, a cyclohexyl group, a norbornyl group, a vinyl group, an allyl group, and a benzyl group.
  • an aromatic polyether polymer refers to a polymer mainly composed of an aromatic ring and containing an ether bond as a mode in which the aromatic ring units are connected.
  • an ether bond there may be a bond mode generally used for forming an aromatic polymer such as a direct bond, ketone, sulfone, sulfide, various alkylenes, imides, amides, esters, and urethanes.
  • the ether bond is preferably at least one per repeating unit of the main constituent component.
  • the aromatic ring may include not only a hydrocarbon aromatic ring but also a hetero ring. Further, a part of the aliphatic units may constitute a polymer together with the aromatic ring unit.
  • Aromatic units include hydrocarbon groups such as alkyl groups, alkoxy groups, aromatic groups, allyloxy groups, halogen groups, nitro groups, cyano groups, amino groups, halogenated alkyl groups, carboxyl groups, phosphonic acid groups, hydroxyl groups, etc. And may have an arbitrary substituent.
  • the aromatic polyether ketone polymer is a general term for polymers having at least an ether bond and a ketone bond in the molecular chain, and is a polyether ketone, a polyether ketone ketone, a polyether ether ketone, a poly ether. It includes ether ether ketone ketone, polyether ketone ether ketone ketone, polyether ketone sulfone, polyether ketone phosphine oxide, polyether ketone nitrile and the like, and does not limit the specific polymer structure.
  • phosphine oxide or nitrile may have insufficient solvent solubility in the ionic group-containing polymer having a protecting group, and if they contain a large amount of sulfone, crystallinity, heat resistant methanol resistance, water resistance, etc. May have insufficient solvent resistance.
  • the segments (A1) and (A2) used in the polymer electrolyte membrane of the present invention are preferably hydrocarbon segments in terms of chemical stability, hot water resistance, and physical durability. Is more preferable, and an aromatic polyether ketone segment is particularly preferable.
  • an aromatic group a segment containing a hydrocarbon-based arylene group such as a phenylene group, a naphthylene group, a biphenylene group, or a fluorenediyl group, a heteroarylene group such as pyridinediyl, quinoxalinediyl, or thiophenediyl is given.
  • a segment containing a hydrocarbon-based arylene group such as a phenylene group, a naphthylene group, a biphenylene group, or a fluorenediyl group
  • a heteroarylene group such as pyridinediyl, quinoxalinediyl, or thiophenediyl is given.
  • the present invention
  • the segment (A2) not containing an ionic group preferably contains a structural unit represented by the following general formula (S2).
  • S2 a structural unit represented by the following general formula (S2).
  • Ar 5 to Ar 8 represent any divalent arylene group, which may be optionally substituted, but does not contain an ionic group.
  • Ar 5 to Ar 8 are independent of each other. Two or more types of arylene groups may be used, and * represents a bonding site with the general formula (S2) or other structural unit.
  • the segment (A1) containing an ionic group contains the structural unit represented by the following general formula (S1).
  • Ar 1 to Ar 4 represent any divalent arylene group, Ar 1 and / or Ar 2 contain an ionic group, and Ar 3 and Ar 4 contain an ionic group Ar 1 to Ar 4 may be optionally substituted, and two or more types of arylene groups may be used independently of each other, and * represents the general formula (S1) or It represents the binding site with other structural units.
  • preferred divalent arylene groups as Ar 1 to Ar 8 are hydrocarbon arylene groups such as phenylene group, naphthylene group, biphenylene group and fluorenediyl group, and heteroarylene groups such as pyridinediyl, quinoxalinediyl and thiophenediyl. Examples include, but are not limited to, groups. Ar 1 and / or Ar 2 contains an ionic group, and Ar 3 and Ar 4 may or may not contain an ionic group. Further, it may be substituted with a group other than an ionic group, but unsubstituted one is more preferable in terms of proton conductivity, chemical stability, and physical durability. Further, a phenylene group containing a phenylene group and an ionic group is preferred, and a p-phenylene group containing a p-phenylene group and an ionic group is most preferred.
  • hydrocarbon arylene groups such as phenylene group, naphthylene group, bipheny
  • the ionic group used in the block copolymer used in the present invention is preferably a negatively charged atomic group, and preferably has a proton exchange capacity.
  • a sulfonic acid group, a sulfonimide group, a sulfuric acid group, a phosphonic acid group, a phosphoric acid group, and a carboxylic acid group are preferably used.
  • the sulfonic acid group is a group represented by the following general formula (f1)
  • the sulfonimide group is a group represented by the following general formula (f2) [in the general formula (f2)
  • R represents an arbitrary organic group .
  • the sulfuric acid group is represented by the following general formula (f3)
  • the phosphonic acid group is represented by the following general formula (f4)
  • the phosphoric acid group is represented by the following general formula (f5) or (f6).
  • the carboxylic acid group means a group represented by the following general formula (f7).
  • Such ionic groups include cases where the functional groups (f1) to (f7) are salts.
  • the cation forming the salt include an arbitrary metal cation, NR 4 + (R is an arbitrary organic group), and the like.
  • R is an arbitrary organic group
  • the valence and the like are not particularly limited and can be used.
  • preferable metal ions include Li, Na, K, Rh, Mg, Ca, Sr, Ti, Al, Fe, Pt, Rh, Ru, Ir, and Pd.
  • Na, K, and Li that are inexpensive and can be easily proton-substituted are more preferably used.
  • ionic groups can be contained in two or more kinds in the polymer electrolyte material, and the combination is appropriately determined depending on the structure of the polymer. Among these, it is more preferable to have at least a sulfonic acid group, a sulfonimide group, and a sulfuric acid group from the viewpoint of high proton conductivity, and most preferable to have at least a sulfonic acid group from the viewpoint of raw material cost.
  • the block copolymer of the present invention has a sulfonic acid group
  • its ion exchange capacity is preferably 0.1 to 5 meq / g, more preferably 1.4 meq / g or more, from the balance of proton conductivity and water resistance. , Most preferably 2 meq / g or more. Moreover, 3.5 meq / g or less is more preferable, Most preferably, it is 3 meq / g or less.
  • the ion exchange capacity is less than 0.1 meq / g, proton conductivity may be insufficient, and when it is greater than 5 meq / g, water resistance may be insufficient.
  • the molar composition ratio (A1 / A2) of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group is proton conduction under low humidification.
  • it is more preferably 0.15 or more, further preferably 0.33 or more, and most preferably 0.5 or more.
  • 5 or less is more preferable, 3 or less is more preferable, and 2.5 or less is the most preferable.
  • the molar composition ratio A1 / A2 is less than 0.15 or exceeds 5, the effect of the present invention may be insufficient, and a lamella or a co-continuous phase separation structure may not be formed, or low humidification conditions. If the proton conductivity below is insufficient, the hot water resistance and physical durability may be insufficient.
  • the molar composition ratio (A1 / A2) represents the ratio of the number of moles of repeating units present in the segment (A1) to the number of moles of repeating units present in the segment (A2).
  • the number average molecular weight of each segment is Means the ratio of the values divided by the molecular weights of the structural units (S1) and (S2), but is not limited to this example.
  • the content of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group is that a phase separation structure is formed.
  • the total is less than 3
  • the sea-island structure or the cylinder structure may appear, and the power generation performance under low humidification, hot water resistance and physical durability are insufficient, and the effects of the present invention cannot be sufficiently obtained. There is.
  • the ion exchange capacity of the segment (A1) containing an ionic group is preferably high from the viewpoint of proton conductivity under low humidification conditions, more preferably 2.5 meq / g or more, and even more preferably 3 meq / g or more, most preferably 3.5 meq / g or more. Moreover, 6.5 meq / g or less is more preferable, 5 meq / g or less is further more preferable, and the most preferable is 4.5 meq / g or less.
  • the ion exchange capacity of the segment (A1) containing an ionic group is less than 2.5 meq / g, proton conductivity under low humidification conditions may be insufficient, and the ion exchange capacity exceeds 6.5 meq / g. Is not preferable because hot water resistance and physical durability may be insufficient.
  • the ion exchange capacity of the segment (A2) containing no ionic group is preferably low from the viewpoint of hot water resistance, mechanical strength, dimensional stability, and physical durability, more preferably 1 meq / g or less, and still more preferably 0.5 meq / g, most preferably 0.1 meq / g or less.
  • the ion exchange capacity of the segment (A2) not containing an ionic group exceeds 1 meq / g, the hot water resistance, mechanical strength, dimensional stability, and physical durability may be insufficient.
  • the ion exchange capacity is the molar amount of sulfonic acid groups introduced per unit dry weight of the block copolymer, polymer electrolyte material, and polymer electrolyte membrane. Indicates a high degree.
  • the ion exchange capacity can be measured by elemental analysis, neutralization titration method or the like. It can also be calculated from the S / C ratio using elemental analysis, but it is difficult to measure when a sulfur source other than sulfonic acid groups is included. Therefore, in the present invention, the ion exchange capacity is defined as a value obtained by the neutralization titration method.
  • the polymer electrolyte material and the polymer electrolyte membrane of the present invention include an embodiment in which the block copolymer of the present invention and other components are included as will be described later. It shall be determined based on the total body volume.
  • the measurement example of neutralization titration is as follows. The measurement is performed three times or more and the average value is taken.
  • Ion exchange capacity [concentration of sodium hydroxide aqueous solution (mmol / mL) ⁇ drop amount (mL)] / dry weight of sample (g)
  • Examples of the method for introducing an ionic group to obtain the block copolymer of the present invention include a method of polymerizing using a monomer having an ionic group and a method of introducing an ionic group by a polymer reaction.
  • a monomer having an ionic group in a repeating unit may be used as a method for polymerizing using a monomer having an ionic group. This method is described in, for example, Journal of Membrane Science, 197, 2002, p.231-242. This method is particularly preferred because it is easy to apply to the control of the ion exchange capacity of the polymer and industrially.
  • Introduction of a phosphonic acid group into an aromatic polymer can be performed by a method described in Polymer Preprints (Polymer Preprints, Japan), 51, 2002, p.
  • Introduction of a phosphate group into an aromatic polymer can be achieved by, for example, phosphoric esterification of an aromatic polymer having a hydroxyl group.
  • Carboxylic acid groups can be introduced into the aromatic polymer by, for example, oxidizing an aromatic polymer having an alkyl group or a hydroxyalkyl group.
  • the introduction of a sulfate group into an aromatic polymer can be achieved by, for example, sulfate esterification of an aromatic polymer having a hydroxyl group.
  • a method for sulfonating an aromatic polymer that is, a method for introducing a sulfonic acid group, for example, the method described in Japanese Patent Laid-Open No. 2-16126 or Japanese Patent Laid-Open No. 2-208322 is used. Can do.
  • an aromatic polymer can be sulfonated by reacting with a sulfonating agent such as chlorosulfonic acid in a solvent such as chloroform, or by reacting in concentrated sulfuric acid or fuming sulfuric acid.
  • a sulfonating agent such as chlorosulfonic acid in a solvent such as chloroform
  • the sulfonating agent is not particularly limited as long as it sulfonates an aromatic polymer, and sulfur trioxide or the like can be used in addition to the above.
  • the degree of sulfonation can be controlled by the amount of sulfonating agent used, the reaction temperature and the reaction time.
  • Introduction of a sulfonimide group into an aromatic polymer can be achieved, for example, by a method of reacting a sulfonic acid group and a sulfonamide group.
  • the segment (A2) not containing an ionic group is more preferably a structural unit that is chemically stable and exhibits crystallinity due to strong intermolecular cohesion.
  • a block copolymer having excellent dimensional stability and physical durability can be obtained.
  • a more preferable specific example of the structural unit represented by the general formula (S2) contained in the segment (A2) that does not contain an ionic group is represented by the following general formula (P1) in terms of raw material availability.
  • a structural unit is mentioned.
  • a structural unit represented by the following formula (S3) is more preferable.
  • the content of the structural unit represented by the general formula (S2) contained in the segment (A2) not containing an ionic group is preferably larger, more preferably 20 mol% or more, and more preferably 50 mol% or more. Is more preferable, and 80 mol% or more is most preferable. When the content is less than 20 mol%, the effects of the present invention on the mechanical strength, dimensional stability, and physical durability due to crystallinity may be insufficient, which is not preferable.
  • segment (A2) not containing an ionic group a preferred example of a structural unit that is copolymerized in addition to the structural unit represented by the general formula (S2) is an aromatic polyether polymer containing a ketone group, What has a structural unit shown by the following general formula (Q1), and does not contain an ionic group is mentioned.
  • Z 1 and Z 2 in the general formula (Q1) each represent a divalent organic group containing an aromatic ring, and each may represent two or more groups, but do not include an ionic group. Each independently represents a positive integer.
  • Preferred organic groups as Z 1 and Z 2 in the general formula (Q1) include Z 1 as a phenylene group and Z 2 as the following general formulas (X-1), (X-2), (X-4) , (X-5) is more preferable. Moreover, although you may substitute by groups other than an ionic group, the direction where it is unsubstituted is more preferable at the point of crystallinity provision.
  • Z 1 and Z 2 are more preferably a phenylene group, and most preferably a p-phenylene group. (The groups represented by the general formulas (X-1), (X-2), (X-4), (X-5) may be optionally substituted with a group other than an ionic group). .
  • the structural unit represented by the general formula (Q1) include structural units represented by the following general formulas (Q2) to (Q7), but are not limited thereto. It is possible to select appropriately in consideration of crystallinity and mechanical strength. Among these, from the viewpoint of crystallinity and production cost, the structural unit represented by the general formula (Q1) is more preferably the following general formulas (Q2), (Q3), (Q6), and (Q7). Formulas (Q2) and (Q7) are most preferable. (General formulas (Q2) to (Q7) are all represented in the para position, but may have other bonding positions such as ortho and meta positions as long as they have crystallinity. The para position is more preferable from the viewpoint of
  • the segment (A1) containing an ionic group is a structural unit that is chemically stable, has an increased acidity due to an electron withdrawing effect, and is introduced with a high density of sulfonic acid groups. Is more preferable, and a block copolymer excellent in proton conductivity under low humidification conditions can be obtained.
  • a more preferable specific example of the structural unit represented by the general formula (S1) contained in the segment (A1) containing an ionic group is represented by the following general formula (P2) in terms of raw material availability.
  • a structural unit is mentioned.
  • a structural unit represented by the following formula (P3) is more preferable, and a structural unit represented by the following formula (S4) is most preferable.
  • content of the structural unit represented by the said general formula (S1) contained in the segment (A2) which does not contain an ionic group the larger one is preferable, 20 mol% or more is more preferable, 50 mol% or more Is more preferable, and 80 mol% or more is most preferable.
  • M 1 to M 4 represent hydrogen, a metal cation, or an ammonium cation, and M 1 to M 4 may represent two or more groups.
  • R1 To r4 each independently represents 0 to 2, r1 + r2 represents 1 to 8, and r1 to r4 may represent two or more numerical values.
  • segment (A1) containing an ionic group a preferred example of a structural unit that is copolymerized in addition to the structural unit represented by the general formula (S1) is an aromatic polyether-based polymer containing a ketone group. The thing containing a sex group is mentioned.
  • the method for synthesizing the segment (A1) containing an ionic group used in the present invention is not particularly limited as long as a substantially sufficient molecular weight can be obtained.
  • an aromatic active dihalide compound and It can be synthesized using an aromatic nucleophilic substitution reaction of a dihydric phenol compound or an aromatic nucleophilic substitution reaction of a halogenated aromatic phenol compound.
  • an aromatic active dihalide compound used in the segment (A1) containing an ionic group the use of a compound in which an ionic acid group is introduced into an aromatic active dihalide compound as a monomer, chemical stability, production cost, ionicity
  • the amount of the group is preferable from the viewpoint that precise control is possible.
  • Specific examples of the monomer having a sulfonic acid group as an ionic group include 3,3′-disulfonate-4,4′-dichlorodiphenylsulfone and 3,3′-disulfonate-4,4′-difluorodiphenyl.
  • a sulfonic acid group is most preferable as an ionic group, but the monomer having an ionic group used in the present invention may have another ionic group.
  • 3,3′-disulfonate-4,4′-dichlorodiphenyl ketone and 3,3′-disulfonate-4,4′-difluorodiphenyl ketone are more preferable from the viewpoint of chemical stability and physical durability. From the viewpoint of polymerization activity, 3,3′-disulfonate-4,4′-difluorodiphenyl ketone is most preferable.
  • the contained segment (A1) further includes a structural unit represented by the following general formula (p1) and is preferably used.
  • the aromatic polyether polymer is a component superior in hot water resistance than the sulfone group, and has dimensional stability, mechanical strength, and physical durability under high temperature and high humidity conditions. It is more preferably used because it is an effective component for an excellent material.
  • These sulfonic acid groups are preferably salted with a monovalent cationic species during polymerization.
  • the monovalent cation species may be sodium, potassium, other metal species, various amines, or the like, but is not limited thereto.
  • These aromatic active dihalide compounds can be used alone, but a plurality of aromatic active dihalide compounds can also be used in combination.
  • M 1 and M 2 represent hydrogen, a metal cation, an ammonium cation, and a1 and a2 each represent an integer of 1 to 4.
  • the structural unit represented by the general formula (p1) is optionally substituted. May be.
  • the aromatic active dihalide compound it is also possible to control the ionic group density by copolymerizing those having an ionic group and those having no ionic group.
  • the segment (A1) containing an ionic group of the present invention it is more preferable not to copolymerize an aromatic active dihalide compound having no ionic group from the viewpoint of ensuring the continuity of the proton conduction path.
  • aromatic active dihalide compound having no ionic group examples include 4,4′-dichlorodiphenylsulfone, 4,4′-difluorodiphenylsulfone, 4,4′-dichlorodiphenylketone, 4,4 Examples include '-difluorodiphenyl ketone, 4,4'-dichlorodiphenylphenylphosphine oxide, 4,4'-difluorodiphenylphenylphosphine oxide, 2,6-dichlorobenzonitrile, 2,6-difluorobenzonitrile, and the like. .
  • 4,4′-dichlorodiphenyl ketone and 4,4′-difluorodiphenyl ketone are more preferable in terms of imparting crystallinity, mechanical strength, physical durability and hot water resistance, and 4,4′-difluoro in terms of polymerization activity.
  • Diphenyl ketone is most preferred.
  • aromatic active dihalide compounds can be used alone, but a plurality of aromatic active dihalide compounds can also be used in combination.
  • a constituent site represented by the following general formula (p2) is further included. It is included and is preferably used.
  • the structural unit is a component that imparts intermolecular cohesion and crystallinity, and is preferably used because it is a material excellent in dimensional stability, mechanical strength, and physical durability under high temperature and high humidity conditions. (The structural unit represented by the general formula (p2) may be optionally substituted, but does not contain an ionic group.)
  • examples of the monomer having no ionic group that can be copolymerized include halogenated aromatic hydroxy compounds.
  • the halogenated aromatic hydroxy compound is not particularly limited, but 4-hydroxy-4′-chlorobenzophenone, 4-hydroxy-4′-fluorobenzophenone, 4-hydroxy-4′-chlorodiphenylsulfone, 4- Hydroxy-4'-fluorodiphenylsulfone, 4- (4'-hydroxybiphenyl) (4-chlorophenyl) sulfone, 4- (4'-hydroxybiphenyl) (4-fluorophenyl) sulfone, 4- (4'-hydroxybiphenyl) ) (4-chlorophenyl) ketone, 4- (4′-hydroxybiphenyl) (4-fluorophenyl) ketone, and the like.
  • these halogenated aromatic hydroxy compounds may be reacted together to synthesize an aromatic polyether compound.
  • segment (A1) containing an ionic group preferred examples of the structural unit that is copolymerized in addition to the structural unit represented by the general formula (S1) are represented by the general formulas (p1) and (p2).
  • An aromatic polyether ketone copolymer comprising the structural units represented by the following general formulas (T1) and (T2) containing the structural units is particularly preferable.
  • A represents a divalent organic group containing an aromatic ring
  • M 5 and M 6 represent hydrogen, a metal cation, and an ammonium cation
  • A represents two or more groups. Is also good.
  • the introduction amount of p1 is based on the total molar amount of T1 and T2, Preferably it is 75 mol% or more, More preferably, it is 90 mol% or more, Most preferably, it is 100 mol%.
  • the introduction amount of p1 is less than 75 mol%, the construction of the proton conduction bus may be insufficient, which is not preferable.
  • divalent organic group A containing an aromatic ring in the general formulas (T1) and (T2) various types that can be used for polymerization of an aromatic polyether polymer by aromatic nucleophilic substitution reaction.
  • a dihydric phenol compound can be used and is not particularly limited.
  • transduced the sulfonic acid group into these aromatic dihydroxy compounds can also be used as a monomer.
  • divalent organic group A containing an aromatic ring examples include groups represented by the following general formulas (X′-1) to (X′-6), but are not limited thereto. Absent. (The groups represented by the formulas (X′-1) to (X′-6) may be optionally substituted.)
  • the number average molecular weight of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group is related to the domain size of the phase separation structure, and the proton conductivity and physical durability at low humidification In view of balance, it is more preferably 5,000 or more, further preferably 10,000 or more, and most preferably 15,000 or more. Moreover, 50,000 or less is more preferable, More preferably, it is 40,000 or less, Most preferably, it is 30,000 or less.
  • the block copolymer is preferably used as a component of the polymer electrolyte membrane of the present invention.
  • the polymer electrolyte membrane refers to one having a thickness that is thin relative to the area, and includes a film and a film-like one.
  • the polymer electrolyte membrane of the present invention When used for a polymer electrolyte fuel cell, it is usually used as a polymer electrolyte membrane or an electrode catalyst layer binder in a membrane state.
  • the polymer electrolyte membrane of the present invention can be applied to various uses.
  • medical applications such as artificial skin, filtration applications, ion exchange resin applications such as chlorine-resistant reverse osmosis membranes, various structural materials applications, electrochemical applications, humidification films, antifogging films, antistatic films, solar cell films It can be applied to a gas barrier film.
  • electrochemical applications include a fuel cell, a redox flow battery, a water electrolysis device, a chloroalkali electrolysis device, and the like, among which the fuel cell is most preferable.
  • Block copolymers consisting of conventional ionic group-containing segments, non-ionic group-containing segments, and linker sites that link the segments are limited due to the synthesis restrictions that require solvent solubility during polymerization and film formation.
  • segments containing ionic groups segments not containing ionic groups were composed of a soluble amorphous polymer. These amorphous segments that do not contain ionic groups are poor in cohesion of polymer molecular chains, so they lack sufficient toughness when formed into a film or cannot fully suppress the swelling of segments that contain ionic groups. , Sufficient mechanical strength and physical durability could not be achieved.
  • due to the problem of the thermal decomposition temperature of the ionic group since cast molding is usually used, a uniform and tough film could not be obtained with a crystalline polymer having poor solubility.
  • the polymer electrolyte membrane of the present invention is composed of a block copolymer having a segment (A2) containing a structural unit represented by the general formula (S2) and not containing an ionic group. Since the segment (A2) not containing the ionic group is a segment showing crystallinity, after molding a block copolymer precursor in which a protective group is introduced into at least the segment (A2) not containing an ionic group, It can be produced by deprotecting at least a part of the protective group contained in the molded product.
  • processability tends to be poor due to crystallization of the polymer in which the domains are formed, rather than random copolymers, so at least a protective group is introduced into the segment (A2) that does not contain ionic groups.
  • a protective group it is preferable to improve processability, and it is preferable to introduce a protective group when the processability of the segment (A1) containing an ionic group is poor.
  • protecting group used in the present invention include protecting groups generally used in organic synthesis, and the protecting group is temporarily introduced on the assumption that it is removed at a later stage. It is a substituent that protects a highly reactive functional group and renders it inactive to the subsequent reaction, and can be deprotected and returned to the original functional group after the reaction. That is, it is paired with a functional group to be protected.
  • a t-butyl group may be used as a hydroxyl-protecting group, but when the same t-butyl group is introduced into an alkylene chain, It is not called a protecting group.
  • the reaction for introducing a protecting group is called protection (reaction), and the reaction for removal is called deprotection (reaction).
  • Such protection reactions include, for example, Theodora W. Greene, “Protective Groups in Organic Synthesis”, John Wiley & Sons, USA. Inc), 1981, which can be preferably used. It can be appropriately selected in consideration of the reactivity and yield of the protection reaction and deprotection reaction, the stability of the protecting group-containing state, the production cost, and the like.
  • the stage for introducing a protecting group in the polymerization reaction may be selected from the monomer stage, the oligomer stage, or the polymer stage, and can be appropriately selected.
  • the protection reaction is more preferably a method in which the ketone moiety is protected / deprotected with a ketal moiety, or the ketone moiety is protected / deprotected with a heteroatom analog of the ketal moiety, such as a thioketal. It is a method to do.
  • the block copolymer used for the polymer electrolyte membrane of the present invention preferably contains at least one selected from the following general formulas (U1) and (U2) as a structural unit containing a protective group.
  • Ar 9 to Ar 12 are any divalent arylene group
  • R 1 and R 2 are at least one group selected from H and an alkyl group
  • R 3 is any An alkylene group
  • E represents O or S, each of which may represent two or more groups, the groups represented by formulas (U1) and (U2) may be optionally substituted.
  • E is O in the general formulas (U1) and (U2) in terms of the odor, reactivity, stability, etc. of the compound, that is, a method for protecting / deprotecting a ketone moiety with a ketal moiety. Most preferred.
  • R 1 and R 2 in the general formula (U1) are more preferably an alkyl group from the viewpoint of stability, more preferably an alkyl group having 1 to 6 carbon atoms, and most preferably an alkyl group having 1 to 3 carbon atoms. It is a group.
  • R 3 in the general formula (U3) is an alkylene group having 1 to 7 carbon atoms in terms of stability, that is, a group represented by C n1 H 2n1 (n1 is an integer of 1 to 7). More preferably, it is an alkylene group having 1 to 4 carbon atoms.
  • R 3 examples include —CH 2 CH 2 —, —CH (CH 3 ) CH 2 —, —CH (CH 3 ) CH (CH 3 ) —, —C (CH 3 ) 2 CH 2 —, — C (CH 3 ) 2 CH (CH 3 ) —, —C (CH 3 ) 2 O (CH 3 ) 2 —, —CH 2 CH 2 CH 2 —, —CH 2 C (CH 3 ) 2 CH 2 — and the like
  • R 3 is at least one selected from —CH 2 CH 2 —, —CH (CH 3 ) CH 2 —, or —CH 2 CH 2 CH 2 — in terms of stability and ease of synthesis. Most preferred.
  • Preferred organic groups as Ar 9 to Ar 12 in the general formulas (U1) and (U2) are a phenylene group, a naphthylene group, or a biphenylene group. These may be optionally substituted.
  • the block copolymer of the present invention is more preferably Ar 11 and Ar 12 in the general formula (U2) are both phenylene groups, and most preferably Ar 11 and Ar in view of solubility and availability of raw materials.
  • Ar 12 is both a p-phenylene group.
  • a method for protecting a ketone moiety with a ketal includes a method in which a precursor compound having a ketone group is reacted with a monofunctional and / or bifunctional alcohol in the presence of an acid catalyst.
  • Alcohol is an aliphatic alcohol having 1 to 20 carbon atoms.
  • An improved method for producing the ketal monomer used in the present invention comprises reacting the ketone precursor 4,4'-dihydroxybenzophenone with a bifunctional alcohol in the presence of an alkyl orthoester and a solid catalyst.
  • the method of deprotecting at least a part of the ketone moiety protected with the ketal to form the ketone moiety is not particularly limited.
  • the deprotection reaction can be performed in the presence of water and acid under non-uniform or uniform conditions, but from the viewpoint of mechanical strength, physical durability, and solvent resistance, after being molded into a film or the like
  • the method of acid treatment with is more preferable.
  • the weight ratio of the acidic aqueous solution necessary for the polymer is preferably 1 to 100 times, but a larger amount of water can be used.
  • the acid catalyst is preferably used at a concentration of 0.1 to 50% by weight of water present.
  • Suitable acid catalysts include strong mineral acids (strong inorganic acids) such as hydrochloric acid, nitric acid, fluorosulfonic acid, sulfuric acid, and strong organic acids such as p-toluenesulfonic acid, trifluoromethanesulfonic acid, and the like.
  • strong mineral acids strong inorganic acids
  • the amount of acid catalyst and excess water, reaction pressure, and the like can be appropriately selected.
  • a film having a film thickness of 25 ⁇ m it can be almost easily obtained by immersing in an acidic aqueous solution as exemplified by a 6N hydrochloric acid aqueous solution and a 5 wt% sulfuric acid aqueous solution and heating at room temperature to 95 ° C. for 1 to 48 hours. The entire amount can be deprotected. Further, even when immersed in a 1N aqueous hydrochloric acid solution at 25 ° C. for 24 hours, substantially all protecting groups can be deprotected.
  • the deprotection conditions are not limited to these, and the deprotection may be performed by acidic gas, organic acid, or heat treatment.
  • the precursors of block copolymers containing the structural units represented by the general formulas (U1) and (U2) are represented by the following general formulas (U1-1) and ( It can be synthesized by an aromatic nucleophilic substitution reaction with an aromatic active dihalide compound using the compound represented by U2-1).
  • the structural units represented by the general formulas (U1) and (U2) may be derived from either the divalent phenol compound or the aromatic active dihalide compound, but the divalent phenol is considered in consideration of the reactivity of the monomer. More preferably, it is derived from a compound.
  • Ar 9 to Ar 12 are any divalent arylene group
  • R 1 and R 2 are at least one group selected from H and an alkyl group
  • R 3 represents an arbitrary alkylene group
  • E represents O or S.
  • the compounds represented by formulas (U1-1) and (U2-1) may be optionally substituted.
  • particularly preferred dihydric phenol compounds used in the present invention include compounds represented by the following general formulas (r1) to (r10), and derivatives derived from these dihydric phenol compounds.
  • compounds represented by general formulas (r4) to (r10) are more preferable from the viewpoint of stability, and more preferable are compounds represented by general formulas (r4), (r5), and (r9).
  • the compound represented by the general formula (r4) is most preferred.
  • a polymer in the oligomer synthesis by the aromatic nucleophilic substitution reaction to obtain the segment used in the present invention, a polymer can be obtained by reacting the monomer mixture in the presence of a basic compound.
  • the polymerization can be carried out in a temperature range of 0 to 350 ° C., but a temperature of 50 to 250 ° C. is preferable. When the temperature is lower than 0 ° C., the reaction does not proceed sufficiently, and when the temperature is higher than 350 ° C., the polymer tends to be decomposed.
  • the reaction can be carried out in the absence of a solvent, but is preferably carried out in a solvent.
  • Solvents that can be used include N, N-dimethylacetamide, N, N-dimethylformamide, N-methyl-2-pyrrolidone, dimethyl sulfoxide, sulfolane, 1,3-dimethyl-2-imidazolidinone, hexamethylphosphontriamide, etc. However, it is not limited to these, and any solvent that can be used as a stable solvent in the aromatic nucleophilic substitution reaction may be used. These organic solvents may be used alone or as a mixture of two or more.
  • Examples of the basic compound include sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, and the like, and those that can convert an aromatic diol into an active phenoxide structure may be used. It can use without being limited to.
  • a crown ether such as 18-crown-6. These crown ethers may be preferably used because they may be coordinated to a sodium ion or potassium ion of a sulfonic acid group to improve the solubility in an organic solvent.
  • water may be generated as a by-product.
  • water can be removed from the system as an azeotrope by coexisting toluene or the like in the reaction system.
  • a water-absorbing agent such as molecular sieve can also be used.
  • Azeotropic agents used to remove reaction water or water introduced during the reaction generally do not substantially interfere with polymerization, co-distill with water and boil between about 25 ° C. and about 250 ° C. Any inert compound.
  • Common azeotropic agents include benzene, toluene, xylene, chlorobenzene, methylene chloride, dichlorobenzene, trichlorobenzene, cyclohexane and the like. Of course, it is beneficial to select an azeotropic agent whose boiling point is lower than that of the dipolar solvent used.
  • An azeotropic agent is commonly used, but it is not always necessary when high reaction temperatures, such as temperatures above 200 ° C., are used, especially when the reaction mixture is continuously sparged with inert gas. In general, it is desirable to carry out the reaction in an inert atmosphere and in the absence of oxygen.
  • the aromatic nucleophilic substitution reaction is carried out in a solvent
  • the amount is less than 5% by weight, the degree of polymerization tends to be difficult to increase.
  • the amount is more than 50% by weight, the viscosity of the reaction system becomes too high, and the post-treatment of the reaction product tends to be difficult.
  • the desired polymer is obtained by removing the solvent from the reaction solution by evaporation and washing the residue as necessary.
  • the reaction solution by adding the reaction solution to a solvent having low polymer solubility and high by-product inorganic salt solubility, the inorganic salt is removed, the polymer is precipitated as a solid, and the polymer is obtained by filtering the precipitate. You can also.
  • the recovered polymer is optionally washed with water, alcohol or other solvent and dried.
  • halide or phenoxide end groups can optionally be reacted by introducing a phenoxide or halide end-capping agent that forms a stable end group.
  • the molecular weight of the block copolymer used in the polymer electrolyte membrane of the present invention is, in terms of polystyrene, a weight average molecular weight of 10,000 to 5,000,000, preferably 10,000 to 500,000. If it is less than 10,000, any of the mechanical strength, physical durability, and solvent resistance may be insufficient, such as cracking in the molded film. On the other hand, if it exceeds 5,000,000, there are problems such as insufficient solubility, high solution viscosity, and poor processability.
  • the chemical structure of the block copolymer used in the polymer electrolyte membrane of the present invention, the infrared absorption spectrum, 1,030 ⁇ 1,045cm -1, S O absorption at 1,160 ⁇ 1,190cm -1 1 , 130 to 1,250 cm ⁇ 1 C—O—C absorption, 1,640 to 1,660 cm ⁇ 1 C ⁇ O absorption, etc., and these composition ratios are determined by neutralization titration of sulfonic acid groups. Or by elemental analysis.
  • the structure can be confirmed from the peak of an aromatic proton of, for example, 6.8 to 8.0 ppm by nuclear magnetic resonance spectrum ( 1 H-NMR). Further, the position and arrangement of sulfonic acid groups can be confirmed by solution 13 C-NMR or solid 13 C-NMR.
  • Specific examples of the method for producing a block copolymer used for the polymer electrolyte membrane of the present invention include a method a. After reacting a dihalide linker with either the segment represented by the formula (S1) having -OM groups at both ends or the segment represented by the formula (S2) having -OM groups at both ends , A method of producing a block copolymer by alternately polymerizing with the other segment, Method b.
  • the segment represented by the formula (S1) having -OM groups at both ends, the segment represented by the formula (S2) having -OM groups at both ends, and a dihalide linker are randomly polymerized to block A method of producing a copolymer, Method c.
  • O in the —OM group represents oxygen
  • M represents H
  • a metal cation or an ammonium cation.
  • the valence and the like are not particularly limited and can be used.
  • Specific examples of preferred metal cations include Li, Na, K, Rh, Mg, Ca, Sr, Ti, Al, Fe, Pt, Rh, Ru, Ir, and Pd. Of these, Na, K, and Li are more preferable.
  • Examples of the —OM group include a hydroxyl group (—OH group), —O ⁇ NR 4 + group (R is H or an organic group), —ONa group, —OK group, —OLi group and the like.
  • the method a is most preferable because the phase separation domain size can be controlled by alternating copolymerization and a chemically stable block copolymer can be produced.
  • the method for producing a block copolymer used for the polymer electrolyte membrane of the present invention includes at least the following steps (1) and (2). By providing these steps, improvement in mechanical strength and durability due to high molecular weight can be achieved, and by alternately introducing both segments, the phase separation structure and domain size are strictly controlled and excellent in low humid proton conductivity. Block copolymer can be obtained.
  • Both -OM groups (M represents H, metal cation, ammonium cation) at both ends of the segment (A1) containing an ionic group, or both segments (A2) containing no ionic group Introducing a linker site into the terminal -OM group; (2) A step of obtaining a block copolymer by polymerizing the linker sites at both ends of the segment and the -OM groups at both ends of the other segment.
  • the linker used in the present invention needs to be a highly reactive compound capable of linking different segments while suppressing randomization and segment cleavage by an ether exchange reaction.
  • Examples include decafluorobiphenyl, hexafluorobenzene, 4,4′-difluorodiphenyl sulfone, and 2,6-difluorobenzonitrile, but the present invention is not limited thereto.
  • a polyfunctional linker such as decafluorobiphenyl or hexafluorobenzene is used, a block copolymer having a branched structure can be produced by controlling the reaction conditions.
  • the halogen atom is represented by F
  • the terminal -OM group is represented by -OK group
  • the alkali metal is represented by Na and K.
  • the present invention is not limited to these. It is possible.
  • the above formula is inserted for the purpose of helping the reader to understand, and does not necessarily accurately represent the chemical structure, exact composition, arrangement, position of the sulfonic acid group, number, molecular weight, etc. of the polymerized components. It is not limited to.
  • a ketal group is introduced as a protecting group for any segment, but in the present invention, it is protected by a component having high crystallinity and low solubility.
  • the segment (A1) containing an ionic group represented by the above formula (H3-1) or (H3-3) does not necessarily require a protective group, and it has durability and dimensional stability. From this viewpoint, those having no protecting group can also be preferably used.
  • the block exemplified by the formula (H3-1) can synthesize an oligomer having a controlled molecular weight by reacting a bisphenol component and an aromatic dihalide component with (N1 + 1): N1.
  • N1 + 1) an aromatic dihalide component
  • the reaction temperature for block copolymerization using a linker is preferably a heating condition of 140 ° C. or lower. More preferably, it is 80 degreeC or more and 120 degrees C or less. By setting the reaction temperature to 120 ° C. or less, randomization of the polymer structure due to the ether exchange reaction during the reaction can be sufficiently suppressed. On the other hand, when the temperature is 80 ° C. or higher, a polymer having a random polymer structure can be obtained.
  • the method of molding the block copolymer into the polymer electrolyte membrane of the present invention in the stage having a protecting group such as ketal, the method of forming a film from a solution state or the method of forming a film from a molten state, etc. Is possible.
  • the former for example, there is a method of forming a film by dissolving the polymer electrolyte material in a solvent such as N-methyl-2-pyrrolidone, casting the solution on a glass plate or the like, and removing the solvent. It can be illustrated.
  • the solvent used for film formation is not particularly limited as long as it can dissolve the block copolymer and then remove it.
  • N, N-dimethylacetamide, N, N-dimethylformamide, N-methyl-2-pyrrolidone Aprotic polar solvents such as dimethyl sulfoxide, sulfolane, 1,3-dimethyl-2-imidazolidinone and hexamethylphosphontriamide, ester solvents such as ⁇ -butyrolactone and butyl acetate, carbonates such as ethylene carbonate and propylene carbonate Solvents, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, propylene glycol monomethyl ether, alkylene glycol monoalkyl ethers such as propylene glycol monoethyl ether, isopropanol, etc.
  • Alcohol solvents, water and mixtures thereof is preferably used, is preferred for high highest solubility aprotic polar solvent.
  • a crown ether such as 18-crown-6.
  • the selection of the solvent is important for the phase separation structure, and an aprotic polar solvent and a low polarity solvent are mixed. It is also a preferred method to use.
  • a tough membrane by subjecting the polymer solution prepared to a required solid content concentration to normal pressure filtration or pressure filtration to remove foreign substances present in the polymer electrolyte solution.
  • the filter medium used here is not particularly limited, but a glass filter or a metallic filter is suitable.
  • the pore size of the minimum filter through which the polymer solution passes is preferably 1 ⁇ m or less. If filtration is not carried out, foreign matter is allowed to enter, and film breakage occurs or durability becomes insufficient.
  • the obtained polymer electrolyte membrane is preferably heat-treated in the state of a metal salt at least part of the ionic group.
  • the polymer electrolyte material to be used is polymerized in the form of a metal salt at the time of polymerization, it is preferable to perform film formation and heat treatment as it is.
  • the metal of the metal salt may be any metal that can form a salt with sulfonic acid, but from the viewpoint of cost and environmental load, Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, Ti, V, Mn, Fe, Co, Ni, Cu, Zn, Zr, Mo, W, and the like are preferable. Among these, Li, Na, K, Ca, Sr, and Ba are more preferable, and Li, Na, and K are more preferable.
  • the temperature of this heat treatment is preferably 80 to 350 ° C., more preferably 100 to 200 ° C., particularly preferably 120 to 150 ° C.
  • the heat treatment time is preferably 10 seconds to 12 hours, more preferably 30 seconds to 6 hours, and particularly preferably 1 minute to 1 hour. If the heat treatment temperature is too low, mechanical strength and physical durability may be insufficient. On the other hand, if it is too high, chemical decomposition of the film material may proceed. If the heat treatment time is less than 10 seconds, the heat treatment effect is insufficient. On the other hand, when it exceeds 12 hours, the film material tends to deteriorate.
  • the polymer electrolyte membrane obtained by the heat treatment can be proton-substituted by being immersed in an acidic aqueous solution as necessary. By forming by this method, the polymer electrolyte membrane of the present invention can achieve both a good balance between proton conductivity and physical durability.
  • a membrane composed of the block copolymer is prepared by the above-described method, and at least a part of the ketone moiety protected by the ketal is removed. It is deprotected to form a ketone moiety. According to this method, it is possible to form a solution film of a block copolymer including a segment that does not contain an ionic group having poor solubility, and it is possible to achieve both proton conductivity, mechanical strength, and physical durability.
  • the film thickness of the polymer electrolyte membrane obtained by the present invention is preferably 1 to 2000 ⁇ m. In order to obtain the mechanical strength and physical durability of the membrane that can withstand practical use, it is more preferably thicker than 1 ⁇ m, and in order to reduce membrane resistance, that is, improve power generation performance, it is preferably thinner than 2000 ⁇ m. A more preferable range of the film thickness is 3 to 50 ⁇ m, and a particularly preferable range is 10 to 30 ⁇ m. Such a film thickness can be controlled by the solution concentration or the coating thickness on the substrate.
  • the polymer electrolyte membrane obtained by the present invention contains additives such as crystallization nucleating agents, plasticizers, stabilizers, antioxidants or mold release agents used in ordinary polymer compounds. It can be added within a range not contrary to the purpose.
  • the polymer electrolyte membrane obtained by the present invention has various polymers, elastomers, and the like for the purpose of improving mechanical strength, thermal stability, workability, etc. within a range that does not adversely affect the above-mentioned various properties. Fillers, fine particles, various additives, and the like may be included. Moreover, you may reinforce with a microporous film, a nonwoven fabric, a mesh, etc.
  • the solid polymer fuel cell has a structure in which a hydrogen ion conductive polymer electrolyte membrane is used as an electrolyte membrane, and a catalyst layer, an electrode base material, and a separator are sequentially laminated on both sides.
  • the catalyst layer laminated on both sides of the electrolyte membrane (that is, the catalyst layer / electrolyte membrane / catalyst layer configuration) is called an electrolyte membrane with a catalyst layer (CCM), and further on both sides of the electrolyte membrane.
  • a catalyst layer and a gas diffusion base material laminated in sequence is an electrode-electrolyte membrane assembly (MEA).
  • MEA electrode-electrolyte membrane assembly
  • a coating method in which a catalyst layer paste composition for forming a catalyst layer is applied and dried on the surface of the electrolyte membrane is generally performed.
  • the electrolytic membrane is swollen and deformed by a solvent such as water or alcohol contained in the paste, and there is a problem that it is difficult to form a desired catalyst layer on the electrolyte membrane surface.
  • the electrolytic membrane is also exposed to a high temperature in the drying step, there is a problem that the electrolytic membrane undergoes thermal expansion or the like and is deformed.
  • the polymer electrolyte membrane obtained by the present invention is tough and excellent in solvent resistance due to crystallinity, it is particularly suitable for use as an electrolyte membrane with a catalyst layer in any of the above coating methods and transfer methods. it can.
  • the temperature and pressure may be appropriately selected depending on the thickness of the electrolyte membrane, the moisture content, the catalyst layer, and the electrode substrate. Further, in the present invention, it is possible to form a composite by pressing even when the electrolyte membrane is in a dry state or in a state of absorbing water.
  • Specific pressing methods include a roll press that defines pressure and clearance, and a flat plate press that defines pressure. From the viewpoint of industrial productivity and suppression of thermal decomposition of a polymer material having an ionic group, it is 0. It is preferably carried out in the range of from °C to 250 °C.
  • the pressurization is preferably as weak as possible from the viewpoint of electrolyte membrane and electrode protection.
  • a pressure of 10 MPa or less is preferable, and the electrode and the electrolyte membrane are stacked without carrying out the complexing by the hot press process.
  • Cell formation is also one of the preferred options from the viewpoint of preventing short-circuiting of the anode and cathode electrodes.
  • this method when power generation is repeated as a fuel cell, the deterioration of the electrolyte membrane presumed to be caused by a short-circuited portion tends to be suppressed, and the durability as a fuel cell is improved.
  • the application of the polymer electrolyte fuel cell using the polymer electrolyte membrane used in the present invention is not particularly limited, but a mobile power supply source is preferable.
  • mobile devices such as mobile phones, personal computers, PDAs, televisions, radios, music players, game machines, headsets, DVD players, human-type and animal-type robots for industrial use, home appliances such as cordless vacuum cleaners, and toys , Electric bicycles, motorcycles, automobiles, buses, trucks and other vehicles and ships, power supplies for mobiles such as railways, stationary primary generators such as stationary generators, or alternatives to these It is preferably used as a hybrid power source.
  • Ion exchange capacity It measured by the neutralization titration method. The measurement was performed 3 times and the average value was taken. 1. After wiping off the moisture on the membrane surface of the electrolyte membrane that had been proton-substituted and thoroughly washed, it was vacuum-dried at 100 ° C. for 12 hours or more to determine the dry weight. 2. To the electrolyte, 50 mL of a 5 wt% aqueous sodium sulfate solution was added and allowed to stand for 12 hours for ion exchange. 3. The generated sulfuric acid was titrated with 0.01 mol / L sodium hydroxide aqueous solution.
  • Ion exchange capacity [concentration of sodium hydroxide aqueous solution (mmol / mL) ⁇ drop amount (mL)] / dry weight of sample (g)
  • a Solartron electrochemical measurement system (Solartron 1287 Electrochemical Interface and Solartron 1255B Frequency Response Analyzer) was used to perform a constant potential impedance measurement by a two-terminal method to determine proton conductivity.
  • the AC amplitude was 50 mV.
  • a sample having a width of 10 mm and a length of 50 mm was used.
  • the measurement jig was made of phenol resin, and the measurement part was opened.
  • a platinum plate (thickness: 100 ⁇ m, 2 sheets) was used. The electrodes were arranged at a distance of 10 mm between the front and back sides of the sample film so as to be parallel to each other and perpendicular to the longitudinal direction of the sample film.
  • N-Methyl-HLC-8022GPC manufactured by Tosoh Corp. is used as an integrated device of an ultraviolet detector and a differential refractometer, and two TSK gel SuperHM-H manufactured by Tosoh Corp. (inner diameter 6.0 mm, length 15 cm) are used as GPC columns.
  • 2-pyrrolidone solvent N-methyl-2-pyrrolidone solvent containing 10 mmol / L of lithium bromide
  • sample concentration 0.1 wt%
  • flow rate 0.2 mL / min
  • temperature 40 ° C.
  • Crystallization calorimetry by differential scanning calorimetry The polymer electrolyte membrane (about 10 mg) as a specimen is pre-dried at a temperature at which sulfonic acid groups do not decompose (for example, 40 to 100 ° C.) to remove moisture After that, the weight is measured. At this time, since the chemical structure or higher order structure of the polymer may change, the temperature is not raised above the crystallization temperature or the thermal decomposition temperature. After measuring the weight, the polymer electrolyte membrane was subjected to a temperature modulation differential scanning calorimetry at the first heating stage under the following conditions.
  • DSC apparatus DSC Q100 manufactured by TA Instruments Measurement temperature range: 25 ° C to thermal decomposition temperature (eg 310 ° C) Temperature increase rate: 5 ° C / min Amplitude: ⁇ 0.796 ° C Sample amount: about 10mg Sample pan: Aluminum crimp pan Measurement atmosphere: Nitrogen 50 mL / min Pre-drying: vacuum drying 60 ° C, 1 hour
  • a value obtained by doubling the amount of heat from the low temperature side to the peak top was calculated as the amount of crystallization heat. Further, since the specimen contained water, the water content was calculated from the detected heat of evaporation of water, and the weight of the polymer electrolyte material was corrected. In addition, the evaporation heat of water is 2277 J / g.
  • Weight of water in sample (g) heat of sample evaporation (J / g) ⁇ sample amount (g) / 2277 (J / g)
  • Crystallization heat amount correction value (J / g) crystallization heat amount (J / g) ⁇ sample amount (g) / (sample amount ⁇ weight of water in sample (g))
  • the degree of crystallinity is obtained by separating each component by performing profile fitting, obtaining the diffraction angle and integrated intensity of each component, and using the obtained crystalline peak and the integrated intensity of the amorphous halo, the following general formula (s2
  • a 100 nm flake was cut at room temperature using an ultramicrotome, and the obtained flake was collected on a Cu grid and subjected to TEM observation. Observation was carried out at an acceleration voltage of 100 kV, and photography was carried out so that the photographic magnifications were x8,000, x20,000, and x100,000. As a device, TEM H7100FA (manufactured by Hitachi, Ltd.) was used.
  • the marker method was applied to the 3D reconstruction process.
  • Au colloidal particles provided on the collodion film were used as alignment markers when performing three-dimensional reconstruction.
  • CT reconstruction is performed based on a total of 124 TEM images acquired from a series of continuous tilted images in which the sample is tilted every 1 ° and the TEM images are taken in the range of + 61 ° to -62 ° with reference to the marker. A three-dimensional phase separation structure was observed.
  • the hot water resistance of the polymer electrolyte membrane was evaluated by measuring the dimensional change rate in hot water at 95 ° C.
  • the electrolyte membrane was cut into a strip having a length of about 5 cm and a width of about 1 cm, immersed in water at 25 ° C. for 24 hours, and the length (L1) was measured with a caliper.
  • the electrolyte membrane was immersed in hot water at 95 ° C. for 8 hours, and then the length (L2) was measured again with a caliper, and the size change was visually observed.
  • Example 1 Synthesis of oligomer a1 ′ not containing an ionic group represented by the following general formula (G3)) (In the formula (G3), m represents a positive integer.)
  • oligomer a1 (terminal: OM group) containing no ionic group.
  • M in the OM group represents Na or K, and the following notation follows this.
  • the number average molecular weight was 10,000.
  • the reaction was carried out at 105 ° C. for 1 hour. Purification was performed by reprecipitation with a large amount of isopropyl alcohol to obtain an oligomer a1 '(terminal: fluoro group) not containing an ionic group represented by the above formula (G3).
  • the number average molecular weight was 11000, and the number average molecular weight of the oligomer a1 'not containing an ionic group was determined to be 10400 obtained by subtracting the linker moiety (molecular weight 630).
  • the block copolymer b1 contains 50 mol% of the structural unit represented by the general formula (S1) as a segment (A1) containing an ionic group, and the segment (A2) containing no ionic group It contained 100 mol% of the structural unit represented by the formula (S2).
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 1.7 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing the ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 5.5. .
  • a crystallization peak was observed in DSC (first heating stage), and the amount of crystallization heat was 26.8 J / g. In addition, no crystalline peak was observed by wide-angle X-ray diffraction (crystallinity 0%).
  • the proton conductivity was 240 mS / cm at 80 ° C. and 85% relative humidity, and 2 mS / cm at 80 ° C. and 25% relative humidity, and was excellent in low humidified proton conductivity. Further, the dimensional change rate was as small as 9%, and the hot water resistance was also excellent.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 18 nm.
  • Example 2 Synthesis of oligomer a3 ′ not containing an ionic group represented by the general formula (G3)
  • Example 1 it changes to the said oligomer a1 (terminal hydroxyl group) which does not contain an ionic group, Example 1 except charging 30.0 g (2 mmol) of the said oligomer a3 (terminal: OM group) which does not contain an ionic group.
  • the oligomer a3 ′ (terminal: fluoro group) not containing the ionic group represented by the formula (G3) was synthesized by the method described.
  • the number average molecular weight was 16000, and the number average molecular weight of the oligomer a3 ′ not containing an ionic group was determined to be 15400 obtained by subtracting the linker moiety (molecular weight 630).
  • the block copolymer b2 contains 50 mol% of the structural unit represented by the general formula (S1) as the segment (A1) containing an ionic group, and the segment (A2) containing no ionic group It contained 100 mol% of the structural unit represented by the formula (S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b2 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 1.5 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing the ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 4.9. .
  • a crystallization peak was observed in DSC (first heating stage), and the crystallization heat amount was 28.2 J / g.
  • no crystalline peak was observed by wide-angle X-ray diffraction (crystallinity 0%).
  • the proton conductivity was 190 mS / cm at 80 ° C. and 85% relative humidity, and 0.8 mS / cm at 80 ° C. and 25% relative humidity, and was excellent in low humidified proton conductivity. Further, the dimensional change rate was as small as 5%, and the hot water resistance was also excellent.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 33 nm.
  • Example 3 Synthesis of oligomer a5 ′ not containing an ionic group represented by the general formula (G3)
  • Example 1 was prepared except that 40.0 g (2 mmol) of the oligomer a5 (terminal: OM group) containing no ionic group was charged instead of the oligomer a1 (terminal: OM group) containing no ionic group.
  • the oligomer a5 ′ (terminal: fluoro group) not containing the ionic group represented by the formula (G3) was synthesized by the method described in (1).
  • the number average molecular weight was 21000, and the number average molecular weight of the oligomer a5 'not containing an ionic group was determined to be 20400, which is obtained by subtracting the linker moiety (molecular weight 630).
  • the block copolymer b3 contains 50 mol% of the structural unit represented by the general formula (S1) as a segment (A1) containing an ionic group, and the segment (A2) containing no ionic group It contained 100 mol% of the structural unit represented by the formula (S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b3 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 1.9 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing the ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 4.7. .
  • a crystallization peak was observed in DSC (first heating stage), and the crystallization heat amount was 30.2 J / g.
  • no crystalline peak was observed by wide-angle X-ray diffraction (crystallinity 0%).
  • the proton conductivity was 290 mS / cm at 80 ° C. and 85% relative humidity, and 4 mS / cm at 80 ° C. and 25% relative humidity, and was excellent in low humidified proton conductivity. Further, the dimensional change rate was as small as 12%, and the hot water resistance was also excellent.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 49 nm.
  • Example 4 Synthesis of oligomer a4 as segment (A1) containing ionic group, oligomer a1 as segment (A2) not containing ionic group, and block copolymer b4 containing octafluorobiphenylene as a linker moiety
  • the method described in Example 1 was used except that 21 g (1 mmol) of an oligomer a4 (terminal: OM group) containing an ionic group was added instead of the oligomer a2 (terminal: OM group) containing an ionic group.
  • the block copolymer b4 was obtained.
  • the weight average molecular weight was 350,000.
  • the block copolymer b4 contains 50 mol% of the structural unit represented by the general formula (S1) as a segment (A1) containing an ionic group, and the segment (A2) containing no ionic group It contained 100 mol% of the structural unit represented by the formula (S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b4 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 2.1 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 5.1. .
  • a crystallization peak was observed by DSC (first heating stage), and the crystallization heat amount was 24.0 J / g.
  • no crystalline peak was observed by wide-angle X-ray diffraction (crystallinity 0%).
  • the proton conductivity was 350 mS / cm at 80 ° C. and 85% relative humidity, and 3 mS / cm at 80 ° C. and 25% relative humidity.
  • the proton conductivity was excellent in low humidification. Further, the dimensional change rate was as small as 13%, and the hot water resistance was also excellent.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 30 nm.
  • Example 5 Synthesis of oligomer a7 containing an ionic group represented by the general formula (G4) Except that the amount of 3,3′-disulfonate-4,4′-difluorobenzophenone was changed to 44.7 g (106 mmol), the ionicity represented by the above formula (G4) was obtained by the method described in Example 1.
  • the oligomer a7 (terminal: OM group) containing a group was obtained.
  • the number average molecular weight was 40,000.
  • the block copolymer b5 contains 50 mol% of the structural unit represented by the general formula (S1) as a segment (A1) containing an ionic group, and the segment (A2) containing no ionic group It contained 100 mol% of the structural unit represented by the formula (S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b5 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 2.7 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 4.3. .
  • a crystallization peak was observed in DSC (first heating stage), and the crystallization heat amount was 25.2 J / g.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 55 nm.
  • Example 1 was prepared except that 20.0 g (2 mmol) of the oligomer a8 (terminal: OM group) not containing an ionic group was charged instead of the oligomer a1 (terminal: OM group) not containing an ionic group.
  • the oligomer a8 ′ (terminal: fluoro group) not containing the ionic group represented by the formula (G5) was synthesized by the method described in (1).
  • the number average molecular weight was 11000, and the number average molecular weight of the oligomer a8 'not containing an ionic group was determined to be 10400 obtained by subtracting the linker moiety (molecular weight 630).
  • the block copolymer b6 contains 50 mol% of the structural unit represented by the general formula (S1) as a segment (A1) containing an ionic group, and the segment (A2) containing no ionic group 50 mol% of the structural unit represented by the formula (S2) was contained.
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b6 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 1.7 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing the ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 3.1. .
  • a crystallization peak was observed in DSC (first heating stage), and the crystallization heat amount was 20.5 J / g.
  • no crystalline peak was observed by wide-angle X-ray diffraction (crystallinity 0%).
  • the proton conductivity was 220 mS / cm at 80 ° C. and 85% relative humidity, and 1 mS / cm at 80 ° C. and 25% relative humidity. The proton conductivity was excellent. Further, the dimensional change rate was relatively small at 21%, and the hot water resistance was excellent.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 23 nm.
  • Example 1 was prepared except that 20.0 g (2 mmol) of the oligomer a9 (terminal: OM group) not containing an ionic group was charged instead of the oligomer a1 (terminal: OM group) not containing an ionic group.
  • the oligomer a9 ′ (terminal: fluoro group) not containing the ionic group represented by the formula (G6) was synthesized by the method described in (1).
  • the number average molecular weight was 11000, and the number average molecular weight of the oligomer a9 'not containing an ionic group was determined to be 10400 obtained by subtracting the linker moiety (molecular weight 630).
  • the block copolymer b7 contains 50 mol% of the structural unit represented by the general formula (S1) as a segment (A1) containing an ionic group, and the segment (A2) containing no ionic group It contained 50 mol% of the structural unit represented by the formula S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b7 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 1.7 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 3.2. .
  • a crystallization peak was observed in DSC (first heating stage), and the crystallization heat amount was 23.5 J / g.
  • no crystalline peak was observed by wide-angle X-ray diffraction (crystallinity 0%).
  • the proton conductivity was 225 mS / cm at 80 ° C. and 85% relative humidity, and 1 mS / cm at 80 ° C. and 25% relative humidity. The proton conductivity was excellent. Further, the dimensional change rate was relatively small at 20%, and the hot water resistance was excellent.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 20 nm.
  • Example 8 Synthesis of oligomer a10 containing an ionic group represented by the following general formula (G7)) (In the formula (G7), M represents Na or K, and n represents a positive integer.)
  • Example 2 The method described in Example 1 was used except that 12.9 g (50 mmol) of K-DHBP and 9.3 g (50 mmol) of 4,4′-biphenol were changed to 25.8 g (100 mmol) of K-DHBP.
  • the oligomer a10 (terminal: OM group) containing an ionic group represented by the following formula (G7) was obtained.
  • the number average molecular weight was 16000.
  • the block copolymer b8 includes the ionic group-containing segment (A1), the structural unit represented by the general formula (S1) as 100 mol%, and the ionic group-free segment (A2) as the segment (A2). It contained 100 mol% of the structural unit represented by the formula (S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b8 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 1.8 meq / g
  • the ketal group remained.
  • the total of the segment (A1) containing the ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 5.4.
  • a crystallization peak was observed by DSC (first temperature raising stage), and the amount of crystallization heat was 27.1 J / g.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 17 nm.
  • Example 9 (Synthesis of oligomer a11 containing an ionic group represented by the general formula (G4)) Except that the amount of 3,3′-disulfonate-4,4′-difluorobenzophenone was changed to 37.5 g (89 mmol), the ionicity represented by the formula (G4) was obtained by the method described in Example 1. Oligomer a11 (terminal: OM group) containing a group was obtained. The number average molecular weight was 5000.
  • the block copolymer b9 contains 50 mol% of the structural unit represented by the general formula (S1) as a segment (A1) containing an ionic group, and the segment (A2) containing no ionic group It contained 100 mol% of the structural unit represented by the formula (S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b9 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 0.8 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 7.1.
  • a crystallization peak was observed in DSC (first heating stage), and the crystallization heat amount was 35.1 J / g.
  • no crystalline peak was observed by wide-angle X-ray diffraction (crystallinity 0%).
  • the proton conductivity was 80 mS / cm at 80 ° C. and 85% relative humidity, and 0.5 mS / cm at 80 ° C. and 25% relative humidity. Further, the dimensional change rate was as small as 3%, and the hot water resistance was excellent.
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 45 nm.
  • Example 10 Synthesis of oligomer a12 ′ not containing an ionic group represented by the general formula (G3)
  • the number average molecular weight was 6000.
  • Example 1 was prepared except that 12.0 g (2 mmol) of the oligomer a12 (terminal: OM group) not containing an ionic group was charged instead of the oligomer a1 (terminal: OM group) containing no ionic group.
  • the oligomer a12 ′ (terminal: fluoro group) not containing the ionic group represented by the formula (G3) was synthesized by the method described in (1).
  • the number average molecular weight was 7000, and the number average molecular weight of the oligomer a12 'not containing an ionic group was determined to be 6400 obtained by subtracting the linker moiety (molecular weight 630).
  • the block copolymer b10 includes the ionic group-containing segment (A1), the structural unit represented by the general formula (S1) as 50 mol%, and the ionic group-free segment (A2) as the segment (A2). 100 mol% of the structural unit represented by the formula ((S2)) was contained.
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b10 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 3.1 meq / g
  • the ketal group remained.
  • the total of the segment (A1) containing an ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 6.5. .
  • a crystallization peak was observed in DSC (first heating stage), and the crystallization heat amount was 20.1 J / g.
  • no crystalline peak was observed by wide-angle X-ray diffraction (crystallinity 0%).
  • phase separation structure was confirmed by TEM and TEM tomography observation, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 70 nm.
  • Comparative Example 1 Synthesis of oligomer a13 ′ not containing an ionic group represented by the general formula (G3)
  • An oligomer a13 (terminal: OM group) containing no ionic group was synthesized by the method described in Example 1 except that the amount of 4,4′-difluorobenzophenone charged was changed to 19.9 g (91 mmol). .
  • the number average molecular weight was 5000.
  • Example 1 was prepared except that 10.0 g (2 mmol) of the oligomer a13 (terminal: OM group) containing no ionic group was charged instead of the oligomer a1 (terminal: OM group) containing no ionic group.
  • the oligomer a13 ′ (terminal: fluoro group) not containing the ionic group represented by the formula (G3) was synthesized by the method described in (1).
  • the number average molecular weight was 6000, and the number average molecular weight of the oligomer a13 'not containing an ionic group was determined to be 5400 obtained by subtracting the linker moiety (molecular weight 630).
  • the block copolymer b11 includes the ionic group-containing segment (A1), the structural unit represented by the general formula (S1) as 50 mol%, and the ionic group-free segment (A2) as the segment (A2). It contained 100 mol% of the structural unit represented by the formula (S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b11 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 3.0 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing the ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 2.3.
  • a crystallization peak was observed by DSC (first heating stage), and the crystallization heat amount was 16.3 J / g.
  • the electrolyte membrane was soft and brittle, and was a transparent and uniform membrane by visual inspection.
  • Proton conductivity is 400 mS / cm at 80 ° C. and 85% relative humidity, and 0.2 mS / cm at 80 ° C. and 25% relative humidity, which is inferior to low humidified proton conductivity compared to Examples 1-10. It was. Further, the dimensional change rate was as large as 80%, and the hot water resistance was inferior.
  • phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 100 nm.
  • the block copolymer b12 contains 50 mol% of the structural unit represented by the general formula (S1) as a segment (A1) containing an ionic group, and the segment (A2) containing no ionic group It contained 100 mol% of the structural unit represented by the formula (S2).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block copolymer b12 was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 0.5 meq / g
  • the remaining ketal group was observed.
  • the total of the segment (A1) containing the ionic group and the segment (A2) containing no ionic group contained in the block copolymer determined from GPC and 1 H-NMR was 2.1. .
  • a crystallization peak was observed by DSC (first heating stage), and the crystallization heat amount was 32.8 J / g.
  • no crystalline peak was observed by wide angle X-ray diffraction (crystallinity 0%).
  • the proton conductivity was 50 mS / cm at 80 ° C. and 85% relative humidity, and 0.05 mS / cm at 80 ° C. and 25% relative humidity.
  • the proton conductivity was inferior to Examples 1-10. Further, the dimensional change rate was as small as 5%, and the hot water resistance was excellent.
  • the hydrophilic domain containing an ionic group did not form a continuous phase in all three slices of the digital slice, and a sea-island-like phase separation structure was confirmed.
  • the period length of the phase separation structure estimated from the autocorrelation function given by the image processing of the TEM image was 250 nm.
  • Comparative Example 4 A polysulfide sulfone block copolymer was synthesized by the method described in Japanese Patent Application Laid-Open No. 2011-23308. First, 25 g (0.15 mol) of diphenyl ether was weighed into an eggplant flask, 60 mL (0.44 mol) of chlorosulfuric acid was slowly added, and the mixture was stirred at room temperature for 2 hours. After completion of the reaction, the reaction solution which had been allowed to cool to room temperature was poured into a total amount of 600 mL of ice to produce a white precipitate. The precipitate was collected by filtration, washed with water, and dried under reduced pressure at 80 ° C. for 7 hours to obtain a crude product of oxobisbenzenesulfonyl chloride.
  • the prepared hydrophilic part oligomer polymerization solution was diluted by adding 8 mL of DMAc and transferred to a flask containing the whole amount of the prepared hydrophobic part oligomer.
  • the system was sufficiently purged with nitrogen, and then polymerized for 36 hours under a heating condition of 175 ° C.
  • DMAc was added and diluted, and then filtered to remove insoluble matters.
  • the obtained filtrate was concentrated and then poured into isopropyl alcohol to precipitate a polymer.
  • sPSS polysulfonated polysulfidesulfone hydrophilic part
  • PSS polysulfidesulfone hydrophobic part
  • MsPSS-PSS-50 sulfonated polysulfidesulfone hydrophilic part
  • the ratio of the hydrophilic part contained in the obtained multi-block polymer is 50 mol%, and the segment (A1) containing the ionic group and the ionic group contained in the block copolymer obtained from GPC and 1 H-NMR The total number of segments (A2) not contained was 4.
  • NMP was added to MBsPSS-PSS-50 obtained above to prepare a 20 wt% solution.
  • This solution was cast on a glass plate and dried under reduced pressure at 60 ° C. for 1 hour and at 50 ° C. for 4 hours to obtain an MBsPSS-PSS (—SO 3 Na) film.
  • the obtained membrane was immersed in 1N hydrochloric acid for one day, washed with ion-exchanged water, and further immersed in ion-exchanged water for one day to protonate the sodium sulfonate in the membrane, and MBsPSS-PSS-50 membrane Got.
  • the ion exchange capacity determined from neutralization titration was 1.9 meq / g.
  • the obtained polymer electrolyte membrane was crystallized in both DSC (first heating stage) and wide-angle X-ray diffraction, and no crystalline peak was observed (amorphous). It was a hard and brittle electrolyte membrane, and was an opaque and non-uniform membrane visually.
  • the proton conductivity is 160 mS / cm at 80 ° C. and a relative humidity of 85%, and 0.1 mS / cm at 80 ° C. and a relative humidity of 25%, which is inferior to the low-humidified proton conductivity as compared with Examples 1 to 10. It was.
  • the dimensional change rate was as large as 80%, and it was inferior to hot water resistance.
  • phase separation structure In TEM and TEM tomography observations, a co-continuous phase separation structure was confirmed, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure accumulated from the autocorrelation function given by the image processing of the TEM image was 22 nm.
  • Comparative Example 5 A polyethersulfone-based block copolymer having a linker was synthesized by the method described in Japanese Patent Application Laid-Open No. 2005-126684. First, 4.31 g (15.0 mmol) of 4,4′-dichlorodiphenylsulfone, 3.05 g (16.4 mmol) of 4,4′-biphenol, potassium carbonate in a one-necked flask equipped with a Dean-Stark tube in a nitrogen atmosphere. 3.39 g (24.5 mmol), NMP 35 mL, and toluene 20 mL were charged, and the water in the system was removed azeotropically by keeping the temperature at 150 ° C. for 2 hours.
  • the manufactured block copolymer was dissolved in NMP, and a polymer electrolyte membrane was formed by the method described in Example 1.
  • the ion exchange capacity determined from neutralization titration was 1.8 meq / g.
  • the obtained polymer electrolyte membrane was crystallized in both DSC (first heating stage) and wide-angle X-ray diffraction, and no crystalline peak was observed (amorphous). Although it was a hard and brittle electrolyte membrane, it was a transparent and uniform membrane by visual observation.
  • the proton conductivity is 140 mS / cm at 80 ° C. and a relative humidity of 85%, and 0.3 mS / cm at 80 ° C. and a relative humidity of 25%, which is inferior to the low-humidified proton conductivity compared to Examples 1 to 10. It was. Further, the dimensional change rate was as large as 55%, and the hot water resistance was poor.
  • phase separation structure a lamellar-like phase separation structure was confirmed, and a continuous phase was formed with both a hydrophilic domain containing an ionic group and a hydrophobic domain containing no ionic group.
  • the period length of the phase separation structure accumulated from the autocorrelation function given by the image processing of the TEM image was 30 nm.
  • Comparative Example 7 A block polymer containing no linker was synthesized according to the method described in International Publication No. 2008-018487.
  • NMP N-methylpyrrolidone
  • the block polymer includes a prepolymer block (S2) having the general formula (G8) as a repeating unit, a repeating formula in which the general formula (G1) is 1, the benzophenone is 0.4, and the disulfonate benzophenone is 0.6. It is composed of a unit block (S1).
  • a polymer electrolyte membrane was formed by the method described in Example 1 using a 25 wt% N-methylpyrrolidone (NMP) solution in which the obtained block polymer was dissolved.
  • NMP N-methylpyrrolidone
  • the ion exchange capacity determined from neutralization titration was 1.7 mmol / g.
  • phase separation structure In TEM and TEM tomography observations, a co-continuous and lamellar-like phase separation structure could not be confirmed, and a part of the phase separation structure lacked uniformity.
  • the period length of the phase separation structure accumulated from the autocorrelation function given by the image processing of the TEM image was 350 nm.
  • Comparative Example 8 A polyether ketone ether sulfone block copolymer having a sulfonic acid group was synthesized by the method described in Japanese Patent Application Laid-Open No. 2005-190830. 99.4 g of 4,4′-dihydroxybenzophenone (4,4′-DHBP) was added to a 2 L three-necked flask equipped with a stirrer, thermometer, condenser, Dean-Stark tube, and nitrogen-introduced three-way cock.
  • the obtained polymerization solution was diluted with NMP and then filtered through Celite, and the filtrate was poured into 1000 mL of a large excess of methanol to coagulate and precipitate.
  • the coagulated product was collected by filtration, air-dried, redissolved in 200 mL of NMP, poured into 1500 mL of a large excess of methanol, and coagulated and precipitated.
  • the coagulated product was collected by filtration and dried under vacuum to obtain 32.1 g of the desired copolymer.
  • the weight average molecular weight in terms of polystyrene determined by G P C was 170,000.
  • the obtained sulfonic acid group-containing polymer was dissolved in NMP, and a polymer electrolyte membrane was formed by the method described in Example 1.
  • the ion exchange capacity determined from neutralization titration was 2.0 meq / g.
  • the obtained polymer electrolyte membrane was crystallized in both DSC (first heating stage) and wide-angle X-ray diffraction, and no crystalline peak was observed (amorphous).
  • the electrolyte membrane was hard and brittle, and was a transparent and uniform membrane visually.
  • Proton conductivity is 170 mS / cm at 80 ° C. and 85% relative humidity, and 0.07 mS / cm at 80 ° C. and 25% relative humidity, which is inferior to low humidified proton conductivity compared to Examples 1-10. It was. Further, the dimensional change rate was as large as 65%, and the hot water resistance was poor.
  • phase separation structure In TEM and TEM tomography observations, a co-continuous and lamellar-like phase separation structure could not be confirmed, and a part of the phase separation structure lacked uniformity. This is thought to be due to the large distribution in the size and arrangement of the hydrophilic and hydrophobic domains because the sulfonic acid groups are introduced at random positions in the polymer skeleton by sulfonation after polymerization. It is done.
  • the period length of the phase separation structure accumulated from the autocorrelation function given by the image processing of the TEM image was 220 nm.
  • the polymer electrolyte membrane of the present invention can be applied to various electrochemical devices (for example, fuel cells, water electrolysis devices, chloroalkali electrolysis devices, etc.). Among these devices, it is suitable for a fuel cell, and particularly suitable for a fuel cell using hydrogen as a fuel.
  • electrochemical devices for example, fuel cells, water electrolysis devices, chloroalkali electrolysis devices, etc.
  • Applications of the polymer electrolyte fuel cell of the present invention are not particularly limited, but are portable devices such as mobile phones, personal computers, PDAs, video cameras, digital cameras, home appliances such as cordless vacuum cleaners, toys, electric bicycles, automatic It is preferably used as a power supply source for vehicles such as motorcycles, automobiles, buses, trucks, etc., moving bodies such as ships, railways, etc., conventional primary batteries such as stationary generators, alternatives to secondary batteries, or hybrid power sources with these. .
  • M1 Co-continuous structure
  • M2 Lamella structure
  • M3 Cylinder structure
  • M4 Sea-island structure

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Abstract

La présente invention se rapporte à une membrane électrolyte polymère qui présente une excellente conductivité protonique même dans des conditions de faible humidification, présente une excellente résistance mécanique et une excellente stabilité chimique et peut obtenir un rendement élevé et une excellente durabilité physique lorsqu'elle est réalisée dans une pile à combustible à polymère solide. Cette membrane électrolyte polymère comprend un copolymère à blocs qui comprend un segment (A1) qui contient un groupe ionique, et/ou un segment (A2) qui ne contient pas un groupe ionique, la membrane électrolyte polymère étant caractérisée par le fait : qu'elle forme une structure à séparation de phases co-continue (M1) ou lamellaire (M2) ; et qu'elle présente une quantité de chaleur de cristallisation égale ou supérieure à 0,1 J/g comme cela est mesuré par une analyse calorimétrique à compensation de puissance, ou un degré de cristallinité égal ou supérieur à 0,5 % comme cela est mesuré par une diffraction des rayons X aux grands angles.
PCT/JP2012/071408 2011-08-29 2012-08-24 Membrane électrolyte polymère, ensemble électrode à membrane qui utilise cette dernière et pile à combustible à polymère solide WO2013031675A1 (fr)

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JP2012539113A JP5338990B2 (ja) 2011-08-29 2012-08-24 高分子電解質膜、それを用いた膜電極複合体および固体高分子型燃料電池
CA2847107A CA2847107C (fr) 2011-08-29 2012-08-24 Membrane electrolyte polymere, ensemble electrode a membrane qui utilise cette derniere et pile a combustible a polymere solide
CN201280041595.4A CN103782434B (zh) 2011-08-29 2012-08-24 高分子电解质膜、使用该高分子电解质膜的膜电极复合体及固体高分子型燃料电池
EP12826803.4A EP2752928B1 (fr) 2011-08-29 2012-08-24 Membrane électrolyte polymère, ensemble électrode à membrane qui utilise cette dernière et pile à combustible à polymère solide
US14/240,754 US20140322628A1 (en) 2011-08-29 2012-08-24 Polymer electrolyte membrane, membrane electrode assembly using same and polymer electrolyte fuel cell
KR1020147005472A KR101409059B1 (ko) 2011-08-29 2012-08-24 고분자 전해질막, 그것을 이용한 막 전극 복합체 및 고체 고분자형 연료 전지

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JP7142796B1 (ja) 2021-03-23 2022-09-27 東レ株式会社 ブロック共重合体、ならびにそれを用いた高分子電解質材料、高分子電解質成型体、高分子電解質膜、触媒層付電解質膜、膜電極複合体、固体高分子型燃料電池および水電解式水素発生装置
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WO2016148017A1 (fr) * 2015-03-13 2016-09-22 東レ株式会社 Membrane à électrolyte polymère composite, ainsi que membrane à électrolyte ayant une couche de catalyseur, ensemble électrode à membrane et pile à combustible polymère solide dans laquelle est utilisée ladite membrane à électrolyte polymère composite
KR20170128252A (ko) 2015-03-13 2017-11-22 도레이 카부시키가이샤 복합 고분자 전해질막, 그리고 그것을 사용한 촉매층 부착 전해질막, 막 전극 복합체 및 고체 고분자형 연료 전지
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WO2022202596A1 (fr) 2021-03-23 2022-09-29 東レ株式会社 Corps moulé en polyélectrolyte, et membrane en polyélectrolyte, membrane électrolytique ayant une couche de catalyseur, ensemble membrane-électrode, pile à combustible de type polymère solide, et dispositif de production d'hydrogène de type électrolyse de l'eau dans lequel ledit corps moulé en polyélectrolyte est utilisé
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JPWO2022202123A1 (fr) * 2021-03-23 2022-09-29
WO2022202123A1 (fr) * 2021-03-23 2022-09-29 東レ株式会社 Copolymère à blocs, son procédé de production, matériau d'électrolyte polymère, article moulé d'électrolyte polymère, film d'électrolyte polymère, film d'électrolyte doté d'une couche de catalyseur, composite d'électrode à membrane, pile à combustible à polymère solide, et dispositif de génération d'hydrogène de type à électrolyse de l'eau
WO2022202122A1 (fr) 2021-03-23 2022-09-29 東レ株式会社 Matériau échangeur de protons, corps moulé échangeur de protons l'utilisant, membrane électrolytique sur laquelle est fixée une couche de catalyseur, ensemble membrane-électrode, pile à combustible à polymère solide et générateur d'hydrogène du type à électrolyse de l'eau
JP2022151724A (ja) * 2021-03-23 2022-10-07 東レ株式会社 ブロック共重合体、ならびにそれを用いた高分子電解質材料、高分子電解質成型体、高分子電解質膜、触媒層付電解質膜、膜電極複合体、固体高分子型燃料電池および水電解式水素発生装置
JP7276600B2 (ja) 2021-03-23 2023-05-18 東レ株式会社 ブロック共重合体およびその製造方法、高分子電解質材料、高分子電解質成型体、高分子電解質膜、触媒層付電解質膜、膜電極複合体、固体高分子型燃料電池ならびに水電解式水素発生装置
KR20230159814A (ko) 2021-03-23 2023-11-22 도레이 카부시키가이샤 고분자 전해질 성형체, 및 그것을 사용한 고분자 전해질막, 촉매층이 형성된 전해질막, 막전극 복합체, 고체 고분자형 연료전지 및 수전해식 수소 발생 장치
KR20230160802A (ko) 2021-03-23 2023-11-24 도레이 카부시키가이샤 고분자 전해질막, 블록 공중합체, 고분자 전해질 재료, 고분자 전해질 성형체, 촉매층을 가진 전해질막, 막전극 복합체, 고체 고분자형 연료 전지 및 수전해식 수소 발생 장치
WO2024058020A1 (fr) * 2022-09-13 2024-03-21 東レ株式会社 Copolymère séquencé, matériau d'électrolyte polymère l'utilisant, article moulé d'électrolyte polymère, membrane électrolytique polymère, membrane électrolytique revêtue de catalyseur, corps composite d'électrode à membrane, pile à combustible à polymère solide et générateur d'hydrogène électrolytique à eau

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CA2847107C (fr) 2017-10-24
CN103782434A (zh) 2014-05-07
CA2847107A1 (fr) 2013-03-07
US20140322628A1 (en) 2014-10-30
EP2752928A1 (fr) 2014-07-09
CN103782434B (zh) 2016-04-20
TW201319102A (zh) 2013-05-16
JP5338990B2 (ja) 2013-11-13
EP2752928A4 (fr) 2015-04-29
JPWO2013031675A1 (ja) 2015-03-23
EP2752928B1 (fr) 2017-11-22
TWI538926B (zh) 2016-06-21
KR101409059B1 (ko) 2014-06-18

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